AUPATFULL (Australia (AU) Patents Full-text)
Subject
Coverage

All patent-relevant areas of science and technology, i.e., all classes of the International
Patent Classification

File Type

Full-Text

Features

ThesauriInternational Patent Classification (/IPC), Cooperative PatentClassification (/CPC), European Patent Classification (/EPC andICO)

Alerts (SDIs)

Weekly or monthly (weekly is the default)

CAS Registry
Numbers® Identifiers



SLART



Keep & Share

Structures

Register Links

RecordContent• Full-text of patent applications, patent specifications, and design patents published inAustralia from 1900 onwards.
• Records are available about 3 days after publication date with the complete content.
• Records of the database contain bibliographic data including patent assignee,inventor, and legal representative information, patent, application and priority
application data, IPC, CPC, and EPC classification codes, abstract, and full-text ofdescription and claims.
• Independent claims and claim groups are searchable for all claims in English.
• Numeric values of 59 physical and chemical properties are searchable in about 20,000
variants of the base and additional units within all full text fields in English.
• Ultimate Owners are searchable in the field /UO and /UOS.
• Standardized and normalized patent assignee names are searched in /PAS and /PAN.
• Key terms, indexed and displayed in the field /KT, enhance retrieval of relevant results,
and make the evaluation of results more efficient. They are useful to broaden searchscope more precisely than Basic Index searches.
• The Locarno classification (/LCL) is available for design patents.
• Database records comprise all documents published for one application.
• Clipped images (mostly front-page images) are also included, when available.
• Some of the full text has been created by Optical Character Recognition (OCR)
software. Therefore, characters may be misinterpreted, or portions of the text may be
incomplete.

File Size• More than 1.8 million family records with more than 2.5 million publications (07/2024)• More than 765,000 front page images from 1913 to present (07/2024)

Coverage1900 to present

Updates

WeeklyLanguage

English

Database
Producer

LexisNexis Business Information Solutions B.V.
Radarweg 291043 NX Amsterdam
The Netherlands
Copyright Holder

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AUPATFULL

Sources

Patent applications and patent specifications published by the Australian Patent Office

User Aids• Online Helps (HELP DIRECTORY lists all help messages available)• STNGUIDE

Clusters• AEROTECH• ALLBIB• AUTHORS• CORPSOURCE• ENGINEERING• FULLTEXT• HPATENTS• NPS• PATENTS• PNTTEXTSTN Database Cluster information

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Search and Display Field Codes
If multiple search terms are linked with an AND operator, all terms are searched in the complete databaserecord, i.e., in all publications referring to one application. For a search in a specific publication of the record,connect the search term and the patent kind code with the (L)-proximity operator, e.g.,
S BOREHOLE/ABEN,TIEN,CLMEN (L) AUA1/PK limits the search to Australian applications AUA1.
Fields that allow left truncation are indicated by an asterisk (*).

General Search Fields
Search Field Name

SearchCode

Search Examples

Display
Codes

Basic Index* (contains single words from title(TIEN), abstract (ABEN), detailed
description (DETDEN), claims (CLMEN),and main claims (MCLMEN), and key terms(KT) fields)

None
or
/BI

S TRANSISTOR AND ELECTRODES ACOUSTIC SENSOR
S ?TRANSFER?

TIEN, ABEN,
DETDEN,
CLMEN,MCLMEN, KT

Abstract*/ABEN(or /AB)
/AN
/AG
/AG.T
/AGA

S BOREHOLE/ABEN

ABEN

S 2010006109/AN
S PATENT ATTORNEY SERVICES/AGS CHRYSILIOU IP, MELBOURNE/AG.T
S 26 ELLINGWORTH PARADE, BOX
HILL/AGAS AU/AG.CNY
S AU/AC

AN
AG
AG
AG

/AD
/AK
/AP
/APO
/AY
/CLMEN (or
/CLM)
/CPC
/CPC.ACDS AD=JAN 2003
S AUA1/AK
S AU 2010-202547 /AP
S AU0000188/APO
S AY>=2000
S DERIVATION/CLMEN

AI
AI
AI
APO
AI
CLMEN

S C12N0009/CPC
S 20121113/CPC.ACD

CPC
CPC.TAB/CPC.KW/CPC.VER/DED/DUPD/DETDEN(or /DETD)/DT (or /TC)
/ED
/EDTX
/EPC.KW/EPC(or /ECLA,/EPCLA)/FA/ICO/ICO.KW/IDT/IPC

S C12N0009/CPC(S)I/CPC.KW
S 20130101/CPC.VER
S 20110124/DED
S 20110111/DUPD
S ?DERIVATION/DETDEN

CPC.TAB
CPC.TABDED
DUPD
DETDENS PATENT/DT
S ED=JULY 2011
S 20110705/EDTXS D12/EPC.KW
S A01B0001-02B/EPC

DT
ED
EDTX
EPC
EPC

S ABEN/FA
S T05B0213-05/ICO
S A4/ICO.KW
S B21K0001-56/IDTS A01B001/IPC/IC/IN(or /AU)/IN.CNY/IPC.ACD
/ICA
/ICI
/IPCI

S A24B/ICS MANDEL W MICKLEY/INS MANDEL?/IN
S AU/IN.CNY
S 20051008/IPC.ACD
S B02C0004-08/ICA
S G07B015-00/ICI
S B21B0001/IPCI

FA
ICO
ICO
IDT
ICM, ICS,IPCI, IPCRIC, ICM, ICS
IN

Accession Number
Agent (5)Agent, Total
Agent Address
Agent Country (WIPO code and text)
Application Country(WIPO code and text)
Application Date (1)Application Kind CodeApplication Number (2)Application Number, Original
Application Year (1)Claims*Cooperative Patent Classification (3)Cooperative Patent Classification,
Action Date
Cooperative Patent Classification, Keywords
Cooperative Patent Classification, Version
Data Entry Date (1)Data Update Date (1)Detailed Description *Document Type
Entry Date (1)Entry Date of Fulltext (1)EPC, Keyword Terms
European Patent Classification (3)Field Availability
ICO (in-computer-only) Classification (3)ICO Keyword Terms
IdT (Indeling der Techniek)
International Patent Classification(ICM, ICS, IPCI, IPCR) (3)International Patent Classification (ICM, ICS)
Inventor
Inventor, Country (WIPO code and text)
IPC, Action Date (1)IPC, Additional
IPC, Initial
IPC, Initial/AG.CNY/AC

AG, AG.CNY
AI

IN, IN.CNY
IPC.TAB
ICA
ICI
IPCI
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General Search Fields (cont’d)Search Field Name
IPC, Keyword Terms
IPC, Main
IPC, Reclassified
IPC, Reform
IPC, Secondary
IPC, Version
Key Terms *Language (code and text)
Language, Filing (code and text)
Locarno Classification
Main Claim*
Number of Claims (1)Number of Paragraphs in DETD
(Detailed Description) (1)Patent Assignee (5)Patent Assignee, Country (WIPO codeand text)
Patent Assignee, Total
Patent Assignee Normalized (5)Patent Assignee Standardized (5)Patent Country
Patent Information Publication Type

SearchCode

Search Examples

Display
Codes/IPC.KW/ICM/IPCR/IPC.REF/ICS/IPC.VER
/KT
/LA
/LAF
/LCL
/MCLMEN(or /MCLM)
/CLMN
/DETN

S INITIAL/IPC.KW
S A01N001/ICM
S B21B0001/IPCR
S A01B0001-04/IPC.REF
S A01B0013-12/ICS
S 7/IPC.VER
S GLUCOCER?/KT
S EN/LAS ENGLISH/LAF
S 99-00/LCL
S ?FRACTURE?/MCLM

IPC.TABICM
IPCR
IPC.TABICS
IPC.TAB
KT
LA
LAF
LCL
MCLMENS 5-7/CLMN
S DETN<10

CLMN
DETN

/PA (or /CS)
/PA.CNY

S BASF AG/PA
S AR/PA.CNY

PA
PA.CNY

/PA.T
/PAN
/PAS
/PC
/PIT

S UNIVERSITY NEVADA/PA.T
S BASF AG/PAN
S BASF AG/PAS
S AU/PCS AUA OPEN TO PUBLICINSPECTION/PITS AUA1/PK
S AU120007/PN
S AU1000101/PNOS AU2009201460B2/PNK
S VOLT/PHP (S) TOUCH SCREEN/BI
S AU/PRCS AUSTRALIA/PRC
S PRD=APRIL 2 2003
S 20030402/PRD
S 20000109/PRDF
S DEA/PRKS DE2000-10001525/PRN
S US03493352/PRNO
S 1993/PRY
S 1993-1994/PRYF
S PD=JAN-FEB 2003
S PY>2003 AND L1
S WO/RLCS WO1995-FR1391/RLN
S 20000109/RLDS PCT APPLICATION/RLT
S 2005/RLY
S WO/RLPCS WO2000000008/RLPN
S 20000309/RLPD
S 2005/RLPY
S FLUID###/TIEN
S BASF/UO
S BASF/UOSS UP=MAR 2023
S 20240503/UPTX

PA.T
PAN
PAS
PI
PIT

Patent Kind CodePatent Number (2)Patent Number, Original
Patent Number/Kind Code
Physical Properties
Priority Country(WIPO code and text)
Priority Date (1)

/PK
/PN
/PNO
/PNK
/PHP
/PRC

Priority Date, First (1)Priority Number Kind CodePriority Number (2)Priority Number, OriginalPriority Year (1)Priority Year, First (1)Publication Date (1)Publication Year (1)Related Application Country
Related Application Number
Related Application Date (1)Related Application Type
Related Application Year (1)Related Patent Country
Related Patent Number
Related Patent Date (1)Related Patent Year (1)Title*
Ultimate Owner (5)Ultimate Owner Standardized (5)Update Date (1)Update Date Text (1)

/PRDF
/PRK
/PRN
/PRNO
/PRY
/PRYF
/PD
/PY
/RLC
/RLN
/RLD
/RLT
/RLY
/RLPC
/RLPN
/RLPD
/RLPY
/TIEN (or /TI)
/UO
/UOS
/UP
/UPTX

/PRD

PI
PI
PNO
PI
KWIC
PRN
PRN
PRN
PRN
PRN
PRNO, PRAO
PRN
PRN
PI
PI
RLI
RLI
RLI
RLI
RLI
RLI
RLI
RLI
RLI
TIEN
UO
UOS
UP
UPTX

(1) Numeric search field that may be searched using numeric operators or ranges.
(2) By default, patent numbers, application and priority numbers are displayed in STN Format. To display them in Derwent format, enter
SET PATENT DERWENT at an arrow prompt. To reset display to STN Format, enter SET PATENT STN.
(3) An online thesaurus is available in this field.
(4) Only valid for IPC version 1–7.
(5) Search with implied (S) proximity is available in this field.
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Super Search Fields
Enter a super search code to execute a search in one or more fields that may contain the desired information.
Super search fields facilitate crossfile and multifile searching. EXPAND may not be used with super search
fields. Use EXPAND with the individual field codes instead.

Search Field Name

SearchCode

FieldsSearched

Display
Codes

Search Examples

Application Number Group/APPS

AP, APO, PRN,
PRNO, RLN

S 2010AU-202547/APPS

AI, APO,
PRAI, PRAO,
APPS

Patent Assignee Group/PASS

PA, PAN, PAS,
PA.T, UO, UOS

S BIONTECH/PASSPA, PAN,PAS, PA.T,
UO, UOSPatent Number Group/PATS

PN, PNO, RLPNS AU2009201460/PATS

PI, PNO, RLPI

Property Fields (1)In AUPATFULL a numeric search for a specific set of physical properties (/PHP) is available within the full-text
fields (TIEN, ABEN, DETDEN and CLMEN). The numeric values are not displayed as single fields but are
instead highlighted within the hit displays.
Use EXPAND/PHP to search for all available physical properties. A search with the respective field codes will
be carried out in all database fields with English text. The /PHP index contains a complete list of codes andrelated text for all physical properties available for numeric search.
Field
Code

Property

Unit

Symbol

/AOS
/BIR
/BIT
/CAP
/CATA
/CDN
/CMOL
/CON
/DB
/DEG
/DEN (/C)
/DEQ
/DOA
/DOS
(/LD50)/DV/ECH(/CHA)/ECO(/ECND)/ELC(/ECC)/ELF(/ECF)/ENE

Amount of substance
Bit Rate
Stored Information
CapacitanceCatalytic Activity
Current Density
Molarity, Molar Concentration
Conductance
DecibelDegreeDensity (Mass Concentration
Dose Equivalent
DosageDose

Mol
Bit/Second
Bit
Farad
Katal
Ampere/Square Meter
Mol/Liter
Siemens
DecibelDegreeKilogram/Cubic Meter
SievertMilligram/Kilogram/Day
Milligram/Kilogram

mol
bit/s
Bit
F
kat
A/m2
mol/L
S
dB
°
kg/m3
Sv
mg/kg/day
mg/kg

S 10 /AOS
S 8000-10000/BIR
S BIT > 3 MEGABIT
S 1-10 MF/CAP
S 1-10/CATAS CDN>10 A/M**2
S UREA/BI (S) 8/CMOLS 1S-3/CON
S DB>50
S CYLINDER/BI (S) 45/DEG
S 5E-3-10E-3/DEN
S 100/DEQ
S 100-300/DOA
S DOS>0.8

Viscosity, dynamic
Electric Charge

Pascal * Second
Coulomb

Pa*s
C

S DV>5000
S 0.0001-0.001/ECH

Electrical Conductivity

Siemens/Meter

S/mElectric Current

AmpereAS ECO>800 S/M (15A)
AQUEOUSS 1-10/ELC

Electric Field

Volt/Meter

V/m

S 200/ELF

Energy

Joule

J

/ERE
(/ERES)/FOR/FRE (/F)

Electrical Resistivity

Ohm*Meter

Ohm*m

S DROPLETS (10A) 40 JOULE 70 JOULE /ENES ERE>0.1

Force
Frequency

NewtonHertz

NHz

S 50 N /FORS OSCILLAT?/BI (S) 1- 3/FRE

Search Examples

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Property Fields(1) (cont’d)
Field
Code

Property

Unit

Symbol

Search Examples

/IU
/KV

International Unit
Viscosity, kinematic

none
Square Meter/Second

IU
m2/s

/LEN (/SIZ)/LUME

Length, Size
Luminous Emittance,
IlluminanceLuminous Flux
Luminous Intensity
Mass
Mass to Charge Ratio
Magnetic Flux Density

Meter
Lux

m
lx

S IU>1000 (P) VITAMIN AS METHYLPOLYSILOXANES/BI(10A) 200-300 CST /KV
S 1-4/LEN
S 10-50/LUME

Lumen
CandelaKilogram
none
Tesla

Lm
cd
kg
m/z
T

S LUMF>1000
S LUMI<4
S ALLOY/BI (30A) 1E-10-1E-5/M
S MCH=1
S MFD>102

Mass Flow Rate

Kilogram/Second

kg/s

S MFR<0.1

Magnetic Field Strength
Molar Mass

Ampere/Meter
Gram/Mol

A/m
g/mol

S 10-20/MFST
S 2000-3000 G/MOL/MM

Molality of Substance

Mol/Kilogram

mol/kgS 01.-10 MOL/KG/MOLS/MVR

Melt Volume Rate,
Melt Flow Ratenone

g/10 minS 3/MVR/PER/PHV (/PH)
/POW
(/PW)
/PPM

Percent (Proportionality)
pH Value
Power

none
pH
Watt

%
pH
W

Parts per million

Ppm

ppm

/PRES (/P)

Pressure

Pascal

Pa

/RAD
/RES
/RI
/RSP

Radioactivity
Electrical ResistanceRefractive Index
Rotational Speed

Becquerel
Ohmnone
Revolution/Minute

Bq
Ohm

/SAR

Area /Surface Area

Square Meter

m2

/SOL
(/SLB)/SSAM

Solubility

Gram/100 gram

g/100gS POLYMER?/AB (5A) 4/PER
S 7.4-7.6/PHVS "HG-XE-?"/BI (S) 100-200
WATT/POW
S 100 PPM /PPM (10A)
ADDITIVE/BI
S (VACUUM (5A) DISTILL?)/BI(S) 1000-1100/PRES
S 10-20/RAD
S SENSOR /BI (S) 10- 100/RES
S 3-4/RIS 2 RPM - 100 RPM /RSP (S)ENGINE/BIS PLATE/BI (S) 10 M**2 - 100
M**2 /SARS SOL>20 G/100G (5A) WATER

Specific Surface Area, Mass

m2/kg

S 1-10/SSAM

/STSC
/TCO
(/TCND)/TEMP (/T)
/TEX
/TIM

Surface Tension
Thermal Conductivity

Square Meter/
Kilogram
Joule /Square Meter
Watt/Meter*Kelvin

J/m2
W/m*K

S 60 J/M**2/STSC
S 1/TCO (S) HEAT?

Temperature
Tex
Time

KelvinGram/Kilometer
SecondK
g/kms/VEL (/V)
/VELA
/VLR

Velocity
Velocity, angular
Volumetric Flow Rate

Meter per Second
Radian/Second
Cubic Meter/Second

m/s
rad/s
m3/s

/VOL
/VOLT

VolumeVoltage

Cubic Meter
Volt

m3
V

S 20-25/TEMP
S 1-5/TEXS ?INCUB?/BI (10A) 50 S - 150
S /TIM
S REDUC?/BI (S) 1E-3-5E-3/VELS VELA>10
S 1 M**3/S - 2 M**3/S /VLR (S)ABRASIVE
S 1E-8-2E-8/VOL.EXS TENSION/BI (10A) 5E-3 V<VOLT<7E-3 V

/LUMF
/LUMI
/M
/MCH
/MFD
(/MFS)/MFR(/MFL)/MFST/MM (/MW,
/MOM)
/MOLS

rpm

(1) Exponential format is recommended for the search of particularly high or low values, e.g., 1.8E+7 or 1.8E7 (for 18000000) and 9.2E-8(for 0.000000092).

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International Patent Classification (/IPC) Thesaurus
The classifications, validity and catchwords for the main headings and subheadings from the current (8th)edition of the WIPO International Patent Classification (IPC) manual are available. The classifications fromthe previous editions (1-7) are also available as separate thesauri. To EXPAND and SEARCH in the thesauri
for editions 1–7, use the field code followed by the edition number, e.g., /IPC2, for the 2nd edition. Catchwords
are included only in the thesauri for the 8th, 7th, 6th , and 5th editions.
Code
ADVANCED(ADV)
ALL
BRO (MAN)BT
CORE (COR)
ED
HIE
INDEX
KT
NEXT
NT
PREV
RT (SIB)
TI

Content

ExamplesAdvanced Codes for the Core Level IPC CodeE A61K0006-02+ADVANCED/IPC

All Associated Terms (BT, SELF, NT, RT)
Complete Class
Broader Term (BT, SELF)
Core Codes for the Advanced Level IPC CodeComplete title of the SELF term and IPC manual edition
Hierarchy Term (Broader and Narrower Term)(BT, SELF, NT)
Complete title of the SELF term
Keyword Term (catchwords) (SELF, KT)
Next Classification
Narrower Terms (SELF, NT)
Previous Classification
Related Terms (SELF, RT)
Complete Title of the SELF Term and Broader Terms(BT, SELF)

E C01C003-00+ALL/IPC
E C01C+BRO/IPC
E C01F001-00+BT/IPC
E G08C0019-22+CORE/IPC
E C01F001-00+ED/IPC
E C01B003-00+HIE/IPC
E C01F001-00+INDEX/IPC
E CYANOGEN+KT/IPC
E C01C001-00+NEXT5/IPC
E C01C+NT/IPC
E C01C001-12+PREV10/IPC
E C01C003-20+RT/IPC
E C01F001-00+TI/IPC

ECLA (/EPC) and ICO Thesauri
These thesauri are available in the /EPC search field (for ECLA codes) and /ICO search field (for'in-computer-only' codes). All relationship codes can be used with both the EXPAND and SEARCH
commands.
Relationship
Code
ALL
AUTO (1)
BT
CODE
DEF
HIE
KT
MAX
NEXT
NEXT(n)NT
PREV
PREV(n)TI

Content

Search Examples

All usually required terms (BT, SELF, CODE, DEF)
Automatic relationship (BT, SELF, CODE, DEF)
Broader terms (BT, SELF)
Classification Code (SELF, CODE)
Definition (SELF, DEF)
Hierarchy terms (all broader and narrower terms) (BT,SELF, DEF, NT)
Keyword terms (SELF, KT)
All associated terms
Next classification within the same class (SELF, NEXT)
Next n classification within the same class
Narrower terms
Previous Code within the same class (SELF, PREV)
Previous n classifications within the same class
Complete Title of the SELF Term and Broader Terms(BT, SELF)

E C12M0001-34H2+ALL/EPC
E G01J003-443+AUTO/EPC
E G01J0003-443+BT/EPC
E SCRAPER BIASING MEANS+CODE/EPC
E B65G0045-16+DEF/EPC
E A01B0001+HIE/EPC
E LASER+KT/EPC
E G01J0003-44B+MAX/EPC
E A01B0001-24+NEXT/EPC
E A01B0001-24+NEXT3/EPC
E G05B0001-04+NT/EPC
E G05B0019-418N1+PREV/EPC
E G05B0019-418N1+PREV2/EPC
E G05B0001-03+TI/EPC(1) Automatic Relationship is SET OFF. In case of SET REL ON the result of EXPAND or SEARCH without any relationship code is thesame as described for AUTO.

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CPC Thesaurus
This thesaurus is available in the /CPC search field. All relationship codes can be used with both the EXPAND
and SEARCH commands.
Relationship CodeALL
AUTO (1)
BT
CODE
DEF
HIE
KT
MAX
NEXT
NEXT(n)NT
PREV
PREV(n)TI

Content
All usually required terms (BT, SELF, CODE, DEF)
Automatic relationship (BT, SELF, CODE, DEF)
Broader terms (BT, SELF)
Classification Code (SELF, CODE)
Definition (SELF, DEF)
Hierarchy terms (all broader and narrower terms) (BT, SELF,
DEF, NT)
Keyword terms (SELF, KT)
All associated terms
Next classification within the same class (SELF, NEXT)
Next n classification within the same class
Narrower terms
Previous Code within the same class (SELF, PREV)
Previous n classifications within the same class
Complete Title of SELF Term and Broader Terms (BT, SELF)

Search Examples
E C12M0001-005+ALL/CPC
E G01J003-443+AUTO/CPC
E G01J0003-443+BT/CPC
E CARTRIDGES+CODE/CPC
E B65G0045-16+DEF/CPC
E A01B0001+HIE/CPC
E LASER+KT/CPC
E G01J0003-44+MAX/CPC
E A01B0001-24+NEXT/CPC
E A01B0001-24+NEXT3/CPC
E G05B0001-04+NT/CPC
E G05B0019-00+PREV/CPC
E G05B0019-00+PREV2/CPC
E G05B0001-03+TI/CPC(1) Automatic Relationship is SET OFF. In case of SET REL ON the result of EXPAND or SEARCH without any relationship code is thesame as described for AUTO.

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AUPATFULLDISPLAY and PRINT Formats

Any combination of formats may be used to display or print answers. Multiple codes must be separated by
spaces or commas, e.g., D L1 1-5 TI AU. The fields are displayed or printed in the order requested.
The information of the latest publication is displayed by default. To display the content for all levels of therecord you can combine all display fields and formats with the qualifier .M except FA, SCAN, and TRIAL. The
default display format is STD.M, i.e., all publication levels of one family in the STD format.
For displaying a particular publication of a database record, you can simply add for certain display field thekind code to the appropriate display format, e.g., ALL.A1. Fields that allow this are indicated by a number (3).
Hit-term highlighting is available for all fields. Highlighting must be ON during SEARCH to use the HIT, KWIC,
and OCC formats.
FormatContent

Examples

ABEN (AB, ABS)
AG
AG.CNY
AI (AP) (1)AN
APO
CLMEN (CLM) (3)
CLMN (2)CPC
CPC.TAB
DETDEN (DETD) (3)
DETN (2)DT (TC)
ED
EDP
EDTX
DED
DUPD
EPC (ECLA, EPCLA)
FA
GI
IC
ICM
ICO
ICS
IDT
IN (AU)IN.CNY
IPC
IPCI
IPCR
LA
LAF
LCL
MCLMEN (MCLM)
PA (CS)
PA.CNYPANPAS
PI (PN) (1)PITPNO
PRN (PRAI) (1,5)
PRNO (PRAO) (2)PRYF
RLI (RLN)TIEN (TI)
UO (5)UOS (5)
UP (1)UPTX (1)Abstract (English)
Agent
Agent, Country
Application Information
Accession Number
Application Number, Original
Claims (English)
Number of Claims
Cooperative Patent Classification
CPC, Tabular
Detailed Description (English)
Number of Paragraphs in DETD
Document Type
Entry Date
Entry Date Patent
Entry Date of Fulltext
Data Entry Date
Data Update Date
European Patent Classification
Field Availability (for all publication levels)
Graphic Image
International Patent Classification (Version 1-7) (ICM, ICS, ICA, ICI)
IPC, Main
ICO (in-computer-only) Classification
IPC, Secondary
IDT Classification
Inventor
Inventor, Country
International Patent Classification (version 1-8) (IPCI, IPCR, ICM, ICS, ICA, ICI)
IPC, Initial
IPC, Reclassified
Language
Language of Filing
Locarno Classification
Main Claim (English)
Patent Assignee
Patent Assignee, Country
Patent Assignee Normalized
Patent Assignee Standardized
Patent Information
Patent Information Publication Type
Patent Number, OriginalPriority Information
Priority Number, OriginalPriority Year, First
Related Patent Information (includes RLPI)
Title (English)
Ultimate Owner
Ultimate Owner Standardized
Update Date
Update Date Text

D TI AB 1-5
D AG
D AG.CNY
D AI
D L3 AND APO
D CLM
D CLMN
D CPC
D CPC.TAB
D DETDD DETN
D DT
D ED
D EDP
D EDTX
D DED
D DUPD
D EPC
D FA
D GI
D IC
D IC
D ICO
D ICS
D IDT
D IN
D IN.CNY
D IPC
D IPCID IPCR
D LA
D LAF
D LCL
D MCLM
D PA
D PA.CNY
D PAN
D PAS
D PI
D PIT
D PNO
D PRN
D PRNOD PRYF
D RLI
D TIEN
D UO
D UOS
D UP
D UPTX
July 2024

10
AUPATFULLDISPLAY and PRINT Formats (cont’d)FormatALL (1,3)
ALLG (1)
IALL (1,3)
DALL (1)
IALLG (1)APPS (1)BIB (1)BIBG (1)
IBIB (1)
IBIBG (1)
BRIEF (1)
BRIEFG (1,4)
IBRIEF (1)IBRIEFG (1,4)
IND
CPC.TABIPC
IPC.TABMAX (ALL.M) (1)
MAXG (ALLG.M) (1)
IMAX (IALL.M) (1)
IMAXG (IALLG.M) 1)
PASS
PATS (1)
SCAN (4)STD (1,6)
STDG (1)ISTD (1)ISTDG (1)
TRIAL (TRI, SAM,SAMPLE, FREE)
TX
HIT
KWIC
OCC

Content

ExamplesAN, EDP, ED, EDTX, UP, DED, DUPD, TIEN, IN, PA, PAS, PAN, UO, UOS,
AG, LAF, LA, DT, PIT, PI, AI, RLI, PRAI, IPC, CPC, EPC, ICO, IDT, LCL
ABEN, DETDEN, CLMEN, KT
ALL, plus graphic image
ALL, indented with text labels
ALL, delimited for post processing
IALL, plus graphic image
AI, RLI, PRAI
AN, EDP, ED, EDTX, UP, DED, DUPD, TIEN, IN, PA, PAS, PAN, UO, UOS, AG,
LAF, LA, DT, PIT, PI, AI, RLI, PRAI, IPC, CPC, EPC, ICO, IDT
BIB, plus graphic image
BIB, indented with text labels
IBIB, plus graphic image
AN, EDP, ED, EDTX, UP, DED, DUPD, TIEN, IN, PA, PAS, PAN, UO, UOS, AG,
LAF, LA, DT, PIT, PI, AI, RLI, PRAI, IPC, EPC, ICO, IDT, LCL, ABEN,MCLMEN, KT
BRIEF, plus graphic image
BRIEF, indented with text labels
BRIEFG, indented with text labels
IPC (ICM, ICS, IPCI, IPCR), CPC, EPC, ICO, IDT, LCL
CPC, CPC.KW, CPC.ACD, CPC.VER in tabular format
International Patent Classification (ICM, ICS, IPCI, IPCR)
IPC, IPC.KW, IPC.ACD, IPC.VER, in tabular version
AN, EDP, ED, EDTX, UP, DED, DUPD, TIEN, IN, PA, PAS, PAN, UO, UOS,
AG, LAF, LA, DT, PIT, PI, AI, RLI, PRAI, IPC, CPC, EPC, ICO, IDT, LCL
ABEN, DETDEN, CLMEN, KT, FA for all levels of publication
MAX, plus graphic image
MAX, indented with text labels
IMAX, plus graphic image
PI, PRAI
PI, PNO, RLPI
TI (random display without answer numbers)
AN, EDP, ED, EDTX, UP, DED, DUPD, TIEN, IN, PA, PAS, PAN, UO, UOS, AG,
LAF, LA, DT, PIT, PI, AI, RLI, PRAI, IPC, CPC, EPC, ICO, IDT, LCL
STD, plus graphic image
STD, indented with text labels
ISTD, plus graphic image
EDP, ED, EDTX, UP, DED, DUPD, TIEN, FA, DETN, CLMN

D ALL

DETDEN, CLMEN

D TX

Hit term(s) and field(s)Up to 50 words before and after hit term(s) (KeyWord-In-Context)
Number of occurrences of hit term(s) and field(s) in which they occur

D HIT
D KWIC
D OCC

D ALLGD IALLD DALLD IALLGD APPS
D BIB
D BIBGD IBIBD IBIBG
D BRIEF
D BRIEFGD IBRIEF
D IBRIEFG
D IND
D CPC.TAB
D IPC
D IPC.TAB
D MAX
D MAXGD IMAXD IMAXG
D PASSD PATSD SCAN
D STD
D STDGD ISTDD ISTDG
D TRIAL(1) By default, patent numbers, application and priority numbers are displayed in STN Format. To display them in Derwent format, enter
SET PATENT DERWENT at an arrow prompt. To reset display to STN Format, enter SET PATENT STN.
(2) Custom display only.
(3) You can combine this display field with the qualifier .PK (Patent Kind Code) to display the content for a certain publication level of arecord, e.g., CLM.B2.
(4) SCAN must be specified on the command line, i.e., D SCAN or DISPLAY SCAN.
(5) If priority information is not available for a certain document, this information is taken from the application information of thisdocument and marked with an asterisk (*).
(6) The default display format is STD.M, i.e., all publication levels of one family in the STD format.

July 2024

11
AUPATFULL

SELECT, ANALYZE, and SORT Fields
The SELECT command is used to create E-numbers containing terms taken from the specified field in ananswer set.
The ANALYZE command is used to create an L-number containing terms taken from the specified field in ananswer set.
The SORT command is used to rearrange the search results in either alphabetic or numeric order of thespecified field(s).
You can combine all fields except FA with the qualifier .M to SELECT/ANALYZE the content of all publicationlevels.
Field Name
Abstract (English)
Agent
Agent, Country
Agent Address
Agent, Total
Accession Number
Application Country
Application Date
Application Information Group
Application Kind CodeApplication Number
Application Number, Original
Application Year
CPC Classification
Data Entry Date
Data Update Date
Document Type
Entry Date
Entry Date Fulltext
Entry Date Patent
European Patent Classification
Field Availability
International Patent Classification
Inventor
Inventor, Country
ICO (in-computer-only) Classification
IdT Classification
IPC (ICM, ICS, ICA, ICI, IPCI, IPCR)
IPC, Additional
IPC, Advanced Level Symbols
IPC, Advanced Level Symbols for Invention
IPC, Core Level
IPC, Core Level, Invention
IPC, Initial
IPC, Initial
IPC, Main
IPC, Reclassified
IPC, Reform
IPC, Secondary
Key Terms
Language
Language of Filing
Locarno Classification
Number of Claims
Number of Paragraphs in DETD
Occurrence Count of Hit Terms
Patent Assignee
Patent Assignee, Country
Patent Assignee, Total

Field CodeABEN (AB)AG
AG.CNY
AGA
AG.T
AN
AC
AD
APPS
AK
AP (AI)
APO
AY
CPC
DED
DUPD
DT (TC)ED
EDTXEDP
EPC (ECLA,EPCLA)FAIC
IN (AU)IN.CNY
ICO
IDT
IPC
ICA
IPC.A
IPC.AI
IPC.C
IPC.CI
ICI
IPCI
ICM
IPCR
IPC.REF
ICS
KT
LA
LAF
LCL
CLMN
DETN
OCC
PA (CS)
PA.CNYPA.T

ANALYZE/
SELECT (1)

SORT

Y
Y
Y
Y
Y
Y
Y
Y
Y
Y (3)
Y (2)
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y

Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
N

Y
Y
Y
Y
Y
Y
Y
Y
Y (4)
Y (4)
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
N
Y
Y
Y

N
N
Y
Y
Y
Y
Y
Y
N
N
N
N
Y
Y
Y
Y
N
Y
N
Y
Y
Y
Y
Y
Y
Y
Y
Y
July 2024

12
AUPATFULL

SELECT, ANALYZE, and SORT Fields (cont’d)Field Name
Patent Assignee Normalized
Patent Assignee Standardized
Patent Country
Patent Information Publication Type
Patent Kind CodePatent Number
Patent Number Group
Patent Number, Original
Patent Number/Kind Code
Pre-IPC8 Symbols from the ICM and first IPC8 values from2006-present
Priority Country
Priority Date
Priority Date, First
Priority Number Kind CodePriority Number
Priority Number, OriginalPriority Year
Priority Year, First
Publication Date
Publication Year
Related Application Country
Related Application Number
Related Application Date
Related Application Year
Related Patent Country
Related Application Number
Related Application Date
Related Application Year
Title (English)
Ultimate Owner Normalized
Ultimate Owner Standardized
Update Date
Update Date Text

ANALYZE/
SELECT (1)

SORT

PAN
PAS
PC
PIT
PK
PN (PI)
PATS
PNO
PNK
IPC.F

Y
Y
Y
Y
Y
Y (default)
Y
Y
Y (3)
Y

Y
Y
Y
Y
Y
Y
Y
Y
Y
N

PRC
PRD
PRDF
PRK
PRN (PRAI)
PRNO
PRY
PRYF
PD
PY
RLC
RLN
RLD
RLY
RLPC
RLPN
RLPD
RLPY
TIEN (TI)
UO
UOS
UP
UPTX

Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y (3)
Y
Y
Y
Y
Y
Y
Y

Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y
Y

Field Code(1) HIT may be used to restrict terms extracted to terms that match the search expression used to create the answer set,e.g., SEL HIT TI.
(2) Selects or analyzes application numbers with /AP appended to the terms created by SELECT.
(3) SELECT or ANALYZE HIT are not valid with this field.
(4) Appends /IPC.REF to the terms created by SELECT.

July 2024

13
AUPATFULL

Sample Records
DISPLAY MAXG (STN format)
AN
TIEN
IN
PA
PAS
UO
UOS
AG
LAF
LA
DT
PI
PIT
AI
PRAI
ICM
IPCI
CPC
EPC
ICO
AB

DETDEN

CLMEN

2009001486
AUPATFULL EDP 20110629 ED 20110629 UP 20200823 EDTX
20110629 UPTX 20200130
DED 20091027 DUPD 20200818 Full-text
Method for producing ethanol from steam exploded sweet potato byfermentation
Chen, Hongzhang; Fu, Xiaoguo; Wang, Weidong
Institute of Process Engineering, Chinese Academy of Sciences
Hu Nan Qiangsheng Medicine Co. Ltd.
INSTITUTE OF PROCESS ENGINEERING CHINESE ACADEMY OF SCIENCES; HU NAN
QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINE
Phillips Ormonde Fitzpatrick, 367 Collins Street, Melbourne, VIC, 3000
EnglishEnglishPatent; (Fulltext)
AU 2009201220
A1
20091015
AUA1 OPEN TO PUBLIC INSPECTION [FROM 20010524 ONWARDS]
AU 2009-201220
A
20090327
CN 2008-10102979
20080328
CN 2008-10102980
20080328
C12P0007-10
C12P0007-10 [I,A]
C12P0007-06; C12P0019-14; Y02E0050-10; C12P0007-10
C12P0007-06; C12P0007-10; C12P0019-14
Y02E0050-16; Y02E0050-17
ocr
The invention provides a method for producing ethanol from steam
exploded sweet potato by fermentation which includes the steps of: 1)
subjecting sweet potato to a steam explosion treatment; 2) subjecting
the sweet potato after the steam explosion to saccharification andfermentation; and 3) collecting ethanol produced by the fermentation. In
the invention, sweet potato is subjected to a pre-treatment utilizing ashort-time, low-pressure steam explosion technology, which omits thelong-time cooking process for the starch-based raw material and reduces
the energy consumption for producing ethanol by fermentation; andbecause the steam explosion treated sweet potato is subjected directly
to saccharification and solid-state fermentation, the water content infermentation mash is reduced greatly so as to increase the concentrationof ethanol in fermentation mash, reduce the energy consumption for…
[DESC0001] METHOD FOR PRODUCING ETHANOL FROM STEAM EXPLODED SWEET POTATOBY FERMENTATION Our Ref : 851019 POF Code: 299774/491920, 491921 The
following statement is a full description of this invention, including
the best method performing it known to applicant(s):Method for Producing Ethanol from Steam Exploded Sweet Potato by
Fermentation This application claims priority from Chinese Application
No.200810102979.8 filed, on 28 March 2008; and from Chinese Application
No.200810102980.0 filed on 28 March 2008; the contents of which are to
be taken as incorporated herein by this reference.
FIELD OF THE INVENTION The present invention relates to a method for
producing ethanol, and particularly, a method for producing ethanol fromsteam exploded sweet potato by fermentation.
BACKGROUND With the rapid development of the human society, theenergy source and resource crisis has become prominent increasingly, and…
[CLM0001] 1. A method for producing ethanol from steam exploded sweet
potato by fermentation, including the steps of:July 2024

14
AUPATFULL[CLM0002] 1) subjecting sweet potato to a steam explosion treatment;[CLM0003] 2) subjecting the sweet potato after the steam explosion tosaccharification and fermentation; and[CLM0004] 3) collecting ethanol produced by the fermentation.
[CLM0005] 2. The method according to claim 1 , wherein the steam
explosion treatment is performed in a steam explosion tank under a steampressure of 0.5-0.8 MPa for 2-4 min.
[CLM0006] 3. The method according to claim 1 , wherein, in the step 2),
the solid-state fermentation is carried out after the saccharificationof the steam exploded sweet potato.
…
AN
TIEN
IN
PA
PAS
UO
UOS
LAF
DT
PI
PIT
AI
PRAI
IPCI
CPC
EPC
ICO
AB

DETDEN

2009001486
AUPATFULL EDP 20110629 ED 20110629 UP 20200816 EDTX
20110629 UPTX 20200128
DED 20101129 DUPD 20200811 Full-text
Method for producing ethanol from steam exploded sweet potato byfermentation
CHEN HONGZHANG; FU XIAOGUO; WANG WEIDONG
INST PROCESS ENG CAS
HU NAN QIANGSHENG MEDICINE CO LTD
INST PROCESS ENG CAS; HU NAN QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINEEnglishPatent; (Fulltext)
AU 2009201220
B2
20101125
AUB2 PATENT PRECEEDED BY A [FROM 19040101 UNTIL 20091231] or PATENTPROCEEDED BY OPI [FROM 20010524 ONWARDS]
AU 2009-201220
A
20090327
CN 2008-10102979
20080328
CN 2008-10102980
20080328
C12P0007-10 [I,A]
C12P0007-06; C12P0019-14; Y02E0050-10; C12P0007-10
C12P0007-06; C12P0007-10; C12P0019-14
Y02E0050-16; Y02E0050-17

Equivalent from US2009246847A1
A method for producing ethanol from steam-exploded sweet potato byfermentation includes subjecting sweet potato to a steam explosion
treatment, subjecting the sweet potato after the steam explosion tosaccharification and fermentation, and collecting ethanol produced by
the fermentation. The sweet potato can optionally be subjected to a
pre-treatment utilizing a short-time, low-pressure steam explosion
technology, which omits the long-time cooking process for the
starch-based raw material and reduces the energy consumption for
producing ethanol by fermentation. The method permits the steam
explosion-treated sweet potato t be subjected directly to…
[DESC0001] METHOD FOR PRODUCING ETHANOL FROM STEAM EXPLODED SWEET POTATOBY FERMENTATION Our Ref : 851019 POF Code: 299774/491920, 491921 The
following statement is a full description of this invention, including
the best method of performing it known to applicant(s):[DESC0002] Oeq O O O O O O Method for Producing Ethanol from Steam
Exploded Sweet Potato by Fermentation FIELD OF THE INVENTION The present
invention relates to a method for producing ethanol, and particularly, amethod for producing ethanol from steam exploded sweet potato byfermentation.
[DESC0003] BACKGROUND A_reference herein to a patent document or other…

July 2024

15
AUPATFULL
CLMEN[CLM0001] 1. A method of producing ethanol from steam exploded sweet
potato by fermentation, including the steps of:[CLM0002] 1) subjecting sweet potato to a steam explosion treatment;
wherein the steam explosion treatment is performed in a steam explosion
tank under a steam pressure of 0.50.8 MPa for 2-4 rain;[CLM0003] 2) subjecting the sweet potato after the steam explosion tosaccharification and fermentation; and[CLM0004] 3) collecting ethanol produced by the fermentation.
[CLM0005] 2. The method according to claim 1 , wherein, in the step 2),
the solid-state fermentation is carried out after the saccharificationof the steam exploded sweet potato.
[CLM0006] 3. The method according to claim 2 , wherein an glucoamylase
is added in an amount of 100-150 U glucoamylase/g dry steam exploded
sweet potato, and the saccharification is performed at 55-60°Cfor
20-60 rain; and then, (NH4 )2 SO4 , K-H2 PO4 and activated yeast areadded, and the fermentation is performed for 48-60 h under a conditionof 30-35°C, wherein, the addition amount of (NH4 )2 SO4 is
0.1-0.15 g (NHa)2 SO4 /]00 g sweet potato, the addition amount of KH2
PO4 is 0.1-0.2 g KHzPO4 /100 g sweet potato, and the addition amount of
said yeast is 0.10-0.30 g yeast/100 g sweet potato.
…

AN
TIEN
IN
PA
PAS
UO
UOS
AG
LAF
LA
DT
PI
PIT
AI
PRAI
ICM
IPCI
CPC
EPC
ICO
AB

2009001486
AUPATFULL EDP 20110629 ED 20110629 UP 20200816 EDTX
20110629 UPTX 20200127
DED 20110124 DUPD 20200811 Full-text
Method for producing ethanol from steam exploded sweet potato byfermentation
Chen, Hongzhang; Fu, Xiaoguo; Wang, Weidong
Institute of Process Engineering, Chinese Academy of Sciences
Hu Nan Qiangsheng Medicine Co. Ltd.
INSTITUTE OF PROCESS ENGINEERING CHINESE ACADEMY OF SCIENCES; HU NAN
QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINEHU NAN QIANGSHENG MEDICINE
Phillips Ormonde Fitzpatrick, 367 Collins Street, Melbourne, VIC, 3000
EnglishEnglishPatent; (Fulltext)
AU 2009201220
B820110120
AUB8 CORRECTED FIRST PAGE OF GRANTED DOC. [FROM 20010524 ONWARDS]
AU 2009-201220
A
20090327
CN 2008-10102979
20080328
CN 2008-10102980
20080328
C12P0007-10
C12P0007-10 [I,A]
C12P0007-06; C12P0019-14; Y02E0050-10; C12P0007-10
C12P0007-06; C12P0007-10; C12P0019-14
Y02E0050-16; Y02E0050-17

ocr
The invention provides a method for producing ethanol from steam
exploded sweet potato by fermentation which includes the steps of: 1)
subjecting sweet potato to a steam explosion treatment; 2) subjecting
the sweet potato after the steam explosion to saccharification andfermentation; and 3) collecting ethanol produced by the fermentation. In
the invention, sweet potato is subjected to a pre-treatment utilizing ashort-time, low-pressure steam explosion technology, which omits thelong-time cooking process for the starch-based raw material and reduces
the energy consumption for producing ethanol by fermentation; and…

July 2024

16
AUPATFULL
DETDEN

CLMEN[DESC0001] METHOD FOR PRODUCING ETHANOL FROM STEAM EXPLODED SWEET POTATOBY FERMENTATION Our Ref : 851019 POF Code: 299774/491920, 491921 The
following statement is a full description of this invention, including
the best method performing it known to applicant(s):Method for Producing Ethanol from Steam Exploded Sweet Potato by
Fermentation FIELD OF THE INVENTION The present invention relates to amethod for producing ethanol, and particularly, a method for producing
ethanol from steam exploded sweet potato by fermentation.
BACKGROUND A_reference herein to a patent document or other matter…
[CLM0001] 1. A method of producing ethanol from steam exploded sweet
potato by fermentation, including the steps of:[CLM0002] 1) subjecting sweet potato to a steam explosion treatment;
wherein the steam explosion treatment is performed in a steam explosion
tank under a steam pressure of 0.50.8 MPa for 2-4 rain;[CLM0003] 2) subjecting the sweet potato after the steam explosion tosaccharification and fermentation; and[CLM0004] 3) collecting ethanol produced by the fermentation.
[CLM0005] 2. The method according to claim 1 , wherein, in the step 2),
the solid-state fermentation is carried out after the saccharificationof the steam exploded sweet potato.
…

KTsweet potato; simultaneous saccharification; solid-state fermentation;
starch cooking; steam explosion tank; energy consumption; biomass fuelethanol; steam explosion treatment; steam explosion technology; drysteam; treated steam; leanness resistant; foodstuff replaceable crop;steam pressure; secondary steam; alcohol concentration; activated yeast;
high starch content; starch type raw material; energy source; resource
crisis; inconvenient traffic; behindhand processing; biomass raw
material; ultraviolet radiation; potential raw material; hubei yichangangel yeast; fermentation mash; water bath; biological ethanol

DISPLAY BRIEFG.M
AN
TIEN
IN
PA
PAS
PAN
AG
DT
PI
PIT
AI
PRAI
RLPI
RLI
IPCI
CPC
EPC
ICO
July 2024

2006008329
AUPATFULL EDP 20110630 ED 20120130 UP 20210510 EDTX
20110630 UPTX 20200127
DED 20110919 DUPD 20200814 Full-text
Pyrolysis method and apparatus
Dam-Johansen, Kim; Jensen, Peter A.; Bech, Niels
Danmarks Tekniske Universitet
DANMARKS TEKNISKE UNIVERSITETDANMARKS TEKNISKE UNIVERSITETFB Rice, Level 23 44 Market Street, Sydney, AU
Patent; (Fulltext)
AU 2006243568
B220110915
AUB2 PATENT PRECEEDED BY A [FROM 19040101 UNTIL 20091231] or PATENTPROCEEDED BY OPI [FROM 20010524 ONWARDS]
AU 2006-243568
A
20060503
US 2005-676959
20050503
EP 2005-76034
20050503
DK2006000241
20060503
WO 2006117005
20061109
WO 2006-DK241
20060503
PCT Application
C10B0053-02 [I,A]; C10B0047-22 [I,A]; C10C0005-00 [I,A]
C10B0053-02; Y02P0020-145; C10C0005-00; C10B0047-22; Y02E0050-10
C10B0047-22; C10B0053-02; C10C0005-00
Y02E0050-14

17
AUPATFULLABMCLMEN

KT

AN
TIEN
IN
PA
PAS
PAN
AG
DT
PI
PIT
AI
PRAI
RLPI
RLI
ICM
ICS
IPCI
CPC

Original
A fast pyrolysis apparatus (200) for producing pyrolysis liquid, such as
oil or tar, char and pyrolysis gas from biomass, such as straw,
comprises a centrifuge chamber (204) and a rotor (210) arranged to
impart rotation on the biomass in the centrifuge chamber to force thebiomass outwardly under the action of centrifugal forces. A furnace(206) arranged coaxially around the centrifuge chamber (204) maintains
the temperature at an outer reactive wall of the centrifuge chamber at
an elevated temperature to effect the pyrolysis process at or near thereactive wall. The apparatus comprises a condenser (218) arranged
coaxially with and surrounded by the centrifuge chamber (204). The
apparatus may be accommodated by a mobile unit for simultaneously
collecting biomass from a field and processing the biomass in theapparatus.
[CLM0001] 1. A method for producing pyrolysis liquid from biomass,
comprising the step of decomposing the biomass into pyrolysis liquid,char and pyrolysis gas in a fast pyrolysis process, the method
comprising the steps of:- feeding the biomass into a centrifuge chamber; - rotating a rotor to
impart rotation on biomass distributed in gas volume in the centrifugechamber, whereby the biomass is forced towards an outer wall of thecentrifuge chamber by centrifugal forces, which centrifugal forces
provide an even pressure of biomass against said outer wall of thecentrifuge chamber; - decomposing the biomass into pyrolysis vapors andchar by maintaining said outer wall at a temperature of 350 - 700
degrees Celsius to effect the pyrolysis process at or near the outerwall of the centrifuge chamber, whereby ablative pyrolysis takes placeat or near said outer wall; - separating the pyrolysis vapours and char;- conveying the pyrolysis vapors and char away from the centrifugechamber; - condensing at least a portion of said pyrolysis vapors to
obtain said pyrolysis liquid and pyrolysis gas.
pyrolysis method; pyrolysis vapour; pyrolysis gas; reactive wall; codeattd abbreviation; pyrolysis centrifuge; pyrolysis chamber; condenser
chamber; pyrolysis process; pyrolysis vapor; pyrolysis liquid; reactor
gas phase temperature; two-letter code; pyrolysis condenser; efficientpyrolysis assembly; heat transmission medium; fast pyrolysis apparatus;
pct gazette; attce note; regular issue; surface pyrolysis; flash
pyrolysis; pyrolysis reaction; reactor wall temperature; centrifugechamber; processing biomass; improved pyrolysis yield; gas phaseretention time; remote pyrolysis facility; art pyrolysis system
2006008329
AUPATFULL EDP 20110630 ED 20110630 UP 20210510 EDTX
20110630 UPTX 20200205
DED 20080111 DUPD 20200814 Full-text
Pyrolysis method and apparatus
Dam-Johansen, Kim; Jensen, Peter A.; Bech, Niels
DANMARKS TEKNISKE UNIVERSITETDANMARKS TEKNISKE UNIVERSITETDANMARKS TEKNISKE UNIVERSITETFB Rice & Co, Level 23 44 Market Street, Sydney, NSW, 2000
Patent; (Fulltext)
AU 2006243568
A2
20061109
AUA2 AMENDED POST OPEN TO PUBLIC INSPECTION [FROM 20010524 ONWARDS]
AU 2006-243568
A
20060503
US 2005-676959
20050503
EP 2005-76034
20050503
DK2006000241
20060503
WO 2006117005
20061109
WO 2006-DK241
20060503
PCT Application
C10B0053-02
C10B0047-22; C10C0005-00
C10B0053-02 [I,A]; C10B0047-22 [I,A]; C10C0005-00 [I,A]
C10B0053-02; Y02P0020-145; C10C0005-00; C10B0047-22; Y02E0050-10
July 2024

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AUPATFULL
EPC
ICO
GI

AB

AN
TIEN
IN
PA
PAS
PAN
AG
DT
PI
PIT
AI
PRAI
RLPI
RLI
IPCI
CPC
EPC
ICO
AB

…
July 2024

C10B0047-22; C10B0053-02; C10C0005-00
Y02E0050-14

ocr(57) Abstract: A fast pyrolysis apparatus (200) for producing pyrolysis
liquid, such as oil or tar, char and pyrolysis gas from biomass, such as
straw, comprises a centrifuge chamber (204) and a rotor (210) arranged
to impart ) rotation on the biomass in the centrifuge chamber to force
the biomass outwardly under the action of centrifugal forces. A furnace(206) arranged coaxially around ti 1 e centrifuge chamber (204)…
2006008329
AUPATFULL EDP 20110630 ED 20120130 UP 20210510 EDTX
20110630 UPTX 20200127
DED 20110919 DUPD 20200814 Full-text
Pyrolysis method and apparatus
Dam-Johansen, Kim; Jensen, Peter A.; Bech, Niels
Danmarks Tekniske Universitet
DANMARKS TEKNISKE UNIVERSITETDANMARKS TEKNISKE UNIVERSITETFB Rice, Level 23 44 Market Street, Sydney, AU
Patent; (Fulltext)
AU 2006243568
B220110915
AUB2 PATENT PRECEEDED BY A [FROM 19040101 UNTIL 20091231] or PATENTPROCEEDED BY OPI [FROM 20010524 ONWARDS]
AU 2006-243568
A
20060503
US 2005-676959
20050503
EP 2005-76034
20050503
DK2006000241
20060503
WO 2006117005
20061109
WO 2006-DK241
20060503
PCT Application
C10B0053-02 [I,A]; C10B0047-22 [I,A]; C10C0005-00 [I,A]
C10B0053-02; Y02P0020-145; C10C0005-00; C10B0047-22; Y02E0050-10
C10B0047-22; C10B0053-02; C10C0005-00
Y02E0050-14
Original
A fast pyrolysis apparatus (200) for producing pyrolysis liquid, such as
oil or tar, char and pyrolysis gas from biomass, such as straw,
comprises a centrifuge chamber (204) and a rotor (210) arranged to
impart rotation on the biomass in the centrifuge chamber to force thebiomass outwardly under the action of centrifugal forces. A furnace(206) arranged coaxially around the centrifuge chamber (204) maintains
the temperature at an outer reactive wall of the centrifuge chamber at
an elevated temperature to effect the pyrolysis process at or near thereactive wall. The apparatus comprises a condenser (218) arranged
coaxially with and surrounded by the centrifuge chamber (204). The
apparatus may be accommodated by a mobile unit for simultaneously
collecting biomass from a field and processing the biomass in theapparatus.

19
AUPATFULLMCLMENKT[CLM0001] 1. A method for producing pyrolysis liquid from biomass,
comprising the step of decomposing the biomass into pyrolysis liquid,char and pyrolysis gas in a fast pyrolysis process, the method
comprising the steps of:- feeding the biomass into a centrifuge chamber; - rotating a rotor to
impart rotation on biomass distributed in gas volume in the centrifugechamber, whereby the biomass is forced towards an outer wall of thecentrifuge chamber by centrifugal forces, which centrifugal forces
provide an even pressure of biomass against said outer wall of thecentrifuge chamber; - decomposing the biomass into pyrolysis vapors andchar by maintaining said outer wall at a temperature of 350 - 700
pyrolysis method; pyrolysis vapour; pyrolysis gas; reactive wall; codeattd abbreviation; pyrolysis centrifuge; pyrolysis chamber; condenser
chamber; pyrolysis process; pyrolysis vapor; pyrolysis liquid; reactor
gas phase temperature; two-letter code; pyrolysis condenser; efficientpyrolysis assembly; heat transmission medium; fast pyrolysis apparatus;
pct gazette; attce note; regular issue; surface pyrolysis; flash
pyrolysis; pyrolysis reaction; reactor wall temperature; centrifugechamber; processing biomass; improved pyrolysis yield; gas phaseretention time; remote pyrolysis facility; art pyrolysis system

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