JP5622576B2 - 減少した水素消費量での再生可能な供給材料からのディーゼル燃料の製造 - Google Patents
減少した水素消費量での再生可能な供給材料からのディーゼル燃料の製造 Download PDFInfo
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Description
[1]
(a)0.1〜30質量%の水を供給材料又は第1の反応区域に加え、ここで水の質量%は全ての再循環流を含む第1の反応区域への全供給流の水の質量%として測定し;
(b)反応条件において水素の存在下で触媒を用いて供給材料を水素化及び脱酸素化し、一酸化炭素及び水を二酸化炭素及び水素に転化することによって第1の反応区域において供給材料を処理し且つ水を処理して、水素、二酸化炭素、及び8〜24個の炭素原子を有するn−パラフィンを含む炭化水素フラクションを含む第1の反応区域の生成物流を与え;
(c)第1の反応区域の生成物流の少なくとも一部を分離して、
(i)水素及び二酸化炭素を含む流れ;
(ii)炭化水素フラクションを含む流れ;及び
(iii)水の流れ;
を形成し;そして
(d)炭化水素フラクションを生成物として回収する;
ことを含む、再生可能な供給材料からパラフィンに富むディーゼル油生成物を製造する方法。
[2]
水の流れの一部を再循環して工程1(a)のための水を与えることを更に含む、[1]に記載の方法。
[3]
少なくともn−パラフィンを含む炭化水素フラクションの一部を、2:1〜8:1の範囲の再循環流:供給材料の体積比で第1の反応区域に再循環することを更に含む、[1]に記載の方法。
[4]
第1の反応区域における反応条件が、40℃〜400℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力を含む、[1]に記載の方法。
[5]
水素及び二酸化炭素を含む流れから二酸化炭素を分離し、残りの水素を第1の反応区域に再循環し、炭化水素フラクションをディーゼル油生成物流並びにナフサ及びLPGの流れに分離し、ナフサ及びLPGの流れをナフサ流及びLPG流に分離することを更に含む、[1]に記載の方法。
[6]
第1の反応区域において石油由来の炭化水素を再生可能な供給材料と共に処理することを更に含む、[1]に記載の方法。
[7]
工程1(c)の前に、加熱高圧水素ストリッパー内で、第1の反応区域の生成物流から水素、水、及び二酸化炭素を含む気体流を分離及び除去し;残りの第1の反応区域の生成物流の一部を第1の反応区域に再循環する;ことを更に含む、[1]に記載の方法。
[8]
水素、水、及び二酸化炭素を含む気体流を少なくとも部分的に分離及び除去した後に、残りの第1の反応区域の生成物流の一部を第2の反応区域に送って、異性化条件において異性化触媒と接触させて、n−パラフィンの少なくとも一部を異性化し、分岐パラフィンに富む流れを生成させることを更に含む、[7]に記載の方法。
[9]
第2の反応区域における異性化条件が、40℃〜400℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力を含む、[8]に記載の方法。
[10]
加熱高圧水素ストリッパーを、40℃〜300℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力で運転する、[8]に記載の方法。
Claims (9)
- (a)0.1〜30質量%の水を供給材料又は第1の反応区域に加え、ここで水の質量%は全ての再循環流を含む第1の反応区域への全供給流の水の質量%として測定し;
(b)反応条件において水素の存在下で触媒を用いて供給材料を水素化及び脱酸素化し、一酸化炭素及び水を二酸化炭素及び水素に転化することによって第1の反応区域において供給材料を処理し且つ水を処理して、水素、二酸化炭素、及び8〜24個の炭素原子を有するn−パラフィンを含む炭化水素フラクションを含む第1の反応区域の生成物流を与え;
(c)第1の反応区域の生成物流の少なくとも一部を分離して、
(i)水素及び二酸化炭素を含む流れ;
(ii)炭化水素フラクションを含む流れ;及び
(iii)水の流れ;
を形成し;そして
(d)炭化水素フラクションを生成物として回収する;
ことを含む、供給材料からパラフィンに富むディーゼル油生成物を製造する方法であって、前記供給材料がグリセリド及び遊離脂肪酸を含む植物又は動物からの油脂であり、前記触媒は水素化及び脱酸素化反応に加えて水性ガスシフト反応を触媒し、第1の反応区域における反応条件が、40℃〜400℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力を含む、方法。 - 水の流れの一部を再循環して工程1(a)のための水を与えることを更に含む、請求項1に記載の方法。
- 少なくともn−パラフィンを含む炭化水素フラクションの一部を、2:1〜8:1の範囲の再循環流:供給材料の体積比で第1の反応区域に再循環することを更に含む、請求項1に記載の方法。
- 水素及び二酸化炭素を含む流れから二酸化炭素を分離し、残りの水素を第1の反応区域に再循環し、炭化水素フラクションをディーゼル油生成物流並びにナフサ及びLPGの流れに分離し、ナフサ及びLPGの流れをナフサ流及びLPG流に分離することを更に含む、請求項1に記載の方法。
- 第1の反応区域において石油由来の炭化水素を供給材料と共に処理することを更に含む、請求項1に記載の方法。
- 工程1(c)の前に、加熱高圧水素ストリッパー内で、第1の反応区域の生成物流から水素、水、及び二酸化炭素を含む気体流を分離及び除去し;残りの第1の反応区域の生成物流の一部を第1の反応区域に再循環する;ことを更に含む、請求項1に記載の方法。
- 水素、水、及び二酸化炭素を含む気体流を少なくとも部分的に分離及び除去した後に、残りの第1の反応区域の生成物流の一部を第2の反応区域に送って、異性化条件において異性化触媒と接触させて、n−パラフィンの少なくとも一部を異性化し、分岐パラフィンに富む流れを生成させることを更に含む、請求項6に記載の方法。
- 第2の反応区域における異性化条件が、40℃〜400℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力を含む、請求項7に記載の方法。
- 加熱高圧水素ストリッパーを、40℃〜300℃の温度、及び689kPa絶対圧(100psia)〜13,790kPa絶対圧(2000psia)の圧力で運転する、請求項7に記載の方法。
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US97381807P | 2007-09-20 | 2007-09-20 | |
US60/973,818 | 2007-09-20 | ||
US12/193,161 | 2008-08-18 | ||
US12/193,161 US7999143B2 (en) | 2007-09-20 | 2008-08-18 | Production of diesel fuel from renewable feedstocks with reduced hydrogen consumption |
PCT/US2008/076947 WO2009039335A1 (en) | 2007-09-20 | 2008-09-19 | Production of diesel fuel from renewable feedstocks with reduced hydrogen consumption |
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US7982075B2 (en) * | 2007-09-20 | 2011-07-19 | Uop Llc | Production of diesel fuel from biorenewable feedstocks with lower hydrogen consumption |
US20090077864A1 (en) * | 2007-09-20 | 2009-03-26 | Marker Terry L | Integrated Process of Algae Cultivation and Production of Diesel Fuel from Biorenewable Feedstocks |
US7915460B2 (en) * | 2007-09-20 | 2011-03-29 | Uop Llc | Production of diesel fuel from biorenewable feedstocks with heat integration |
US7982077B2 (en) * | 2007-09-20 | 2011-07-19 | Uop Llc | Production of diesel fuel from biorenewable feedstocks with selective separation of converted oxygen |
US7982078B2 (en) * | 2007-09-20 | 2011-07-19 | Uop Llc | Production of diesel fuel from biorenewable feedstocks with selective separation of converted oxygen |
US7982076B2 (en) * | 2007-09-20 | 2011-07-19 | Uop Llc | Production of diesel fuel from biorenewable feedstocks |
US8124572B2 (en) * | 2007-09-27 | 2012-02-28 | Chevron U.S.A. Inc. | Production of biofuels and biolubricants from a common feedstock |
US7815694B2 (en) * | 2007-09-27 | 2010-10-19 | Chevron U.S.A. Inc. | Production of biofuels and biolubricants from a common feedstock |
WO2009025542A1 (en) | 2008-02-26 | 2009-02-26 | Ruslee Hussain | Improved process of refining crude vegetable oil and animal fats for biodiesel feedstock |
-
2008
- 2008-08-18 US US12/193,161 patent/US7999143B2/en not_active Expired - Fee Related
- 2008-09-19 BR BRPI0816888A patent/BRPI0816888A2/pt not_active IP Right Cessation
- 2008-09-19 JP JP2010525988A patent/JP5622576B2/ja not_active Expired - Fee Related
- 2008-09-19 CA CA2699897A patent/CA2699897C/en not_active Expired - Fee Related
- 2008-09-19 AR ARP080104081A patent/AR068494A1/es active IP Right Grant
- 2008-09-19 WO PCT/US2008/076947 patent/WO2009039335A1/en active Application Filing
- 2008-09-19 EP EP08832287A patent/EP2188354A4/en not_active Withdrawn
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EP2188354A1 (en) | 2010-05-26 |
WO2009039335A1 (en) | 2009-03-26 |
US7999143B2 (en) | 2011-08-16 |
CA2699897A1 (en) | 2009-03-26 |
CA2699897C (en) | 2014-09-09 |
JP2010540700A (ja) | 2010-12-24 |
AR068494A1 (es) | 2009-11-18 |
EP2188354A4 (en) | 2012-12-05 |
BRPI0816888A2 (pt) | 2017-05-23 |
US20090077867A1 (en) | 2009-03-26 |
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