RADIATION STERILIZATION-RESISTANT PROTEIN COMPOSITION
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United States of America Patent
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Issued Date -
May 14, 2015
app pub date -
May 13, 2013
filing date -
May 14, 2012
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Abstract
A protein composition which comprises a mixture of glycine, phenylalanine and histidine and/or a cellulose ether derivative as an additive and has resistance to radiation sterilization.
First Claim
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- 15 United States
- 10 France
- 8 Japan
- 7 China
- 5 Korea
- 2 Other
Patent Owner(s)
Patent Owner | Address | |
---|---|---|
TEIJIN LIMITED | 2-4 NAKANOSHIMA 3-CHOME KITA-KU OSAKA-SHI OSAKA 5300005 ?5300005 |
International Classification(s)

- 2013 Application Filing Year
- A61K Class
- 12711 Applications Filed
- 11051 Patents Issued To-Date
- 86.95 % Issued To-Date
Inventor(s)
Inventor Name | Address | # of filed Patents | Total Citations |
---|---|---|---|
Akiyama, Yusuke | Tokyo, JP | 18 | 41 |
# of filed Patents : 18 Total Citations : 41 | |||
Fujinaga, Kentaro | Tokyo, JP | 8 | 34 |
# of filed Patents : 8 Total Citations : 34 | |||
Hirashima, Masaki | Kikuchi-shi, JP | 24 | 130 |
# of filed Patents : 24 Total Citations : 130 | |||
Honda, Susumu | Tokyo, JP | 77 | 1249 |
# of filed Patents : 77 Total Citations : 1249 | |||
Ishiwari, Ayumi | Tokyo, JP | 5 | 8 |
# of filed Patents : 5 Total Citations : 8 | |||
Kageyama, Yukako | Tokyo, JP | 6 | 19 |
# of filed Patents : 6 Total Citations : 19 | |||
Kaneko, Hiroaki | Tokyo, JP | 82 | 1043 |
# of filed Patents : 82 Total Citations : 1043 | |||
Katou, Souichirou | Tokyo, JP | 1 | 2 |
# of filed Patents : 1 Total Citations : 2 | |||
Kimura, Yukiko | Tokyo, JP | 1 | 2 |
# of filed Patents : 1 Total Citations : 2 | |||
Satake, Makoto | Tokyo, JP | 32 | 149 |
# of filed Patents : 32 Total Citations : 149 | |||
Yamaguchi, Ayuko | Tokyo, JP | 5 | 17 |
# of filed Patents : 5 Total Citations : 17 |
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Patent Citation Ranking
- 2 Citation Count
- A61K Class
- 31.06 % this patent is cited more than
- 10 Age
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Maintenance Fees
Fee | Large entity fee | small entity fee | micro entity fee | due date |
---|---|---|---|---|
11.5 Year Payment | $7400.00 | $3700.00 | $1850.00 | Nov 14, 2026 |
Fee | Large entity fee | small entity fee | micro entity fee |
---|---|---|---|
Surcharge - 11.5 year - Late payment within 6 months | $160.00 | $80.00 | $40.00 |
Surcharge after expiration - Late payment is unavoidable | $700.00 | $350.00 | $175.00 |
Surcharge after expiration - Late payment is unintentional | $1,640.00 | $820.00 | $410.00 |
Full Text
US Patent Application No: 2016/0367,960
METHOD AND SYSTEM FOR CARRYING OUT AN EXOTHERMIC GAS PHASE REACTION ON A HETEROGENEOUS PARTICULATE CATALYST
Abstract
The invention relates to a method for producing 1,3 butadien by means of the oxidative dehydration of n-butenes on a heterogenous particulate multimetal oxide catalyst which contains molybdenum as the active compound and at least one other metal and which is filled into the contact tubes (KR) of two or more tube bundle reactors (R-I, R-II), wherein a heat transfer medium flows around the intermediate space between the contact tubes (KR) of the two or more tube bundle reactors (R-I, R-II). The method includes a production mode and a regeneration mode which are carried out in an alternating manner. In the production mode, an n-butene-containing feed flow is mixed with an oxygen-containing gas flow and conducted as a supply flow (1) over the heterogenous particulate multimetal oxide catalyst filled into the contact tubes (KR) of the two or more tube bundle reactors (R-I, R-II), and the heat transfer medium absorbs the released reaction heat, minus the heat quantity used to heat the supply flow (1) to the reaction temperature in the production mode, by means of an indirect heat exchange and completely or partly dispenses the reaction heat onto a secondary heat transfer medium (H2Oliq) in an external cooler (SBK). In the regeneration mode, the heterogenous particulate multimetal oxide catalyst is regenerated by conducting an oxygen-containing gas mixture (3) over the catalyst and burning off the deposits accumulated on the heterogenous particulate multimetal oxide catalyst. The invention is characterized in that the two or more tube bundle reactors (R-I, R-II) have a single heat transfer medium circuit and as many of the two or more tube bundle reactors (R-I, R-II) as necessary are operated constantly in the production mode so that the released reaction heat, minus the heat quantity used to heat the supply flow (1) to the reaction temperature in the production mode, suffices to keep the temperature of the heat transfer medium in the intermediate spaces between the content tubes (KR) of all the tube bundle reactors (R-I, R-II) at a constant level with a variation range of maximally +/−10 DEG C.
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