GB406345A - Improvements in or relating to the production of formic acid - Google Patents

Improvements in or relating to the production of formic acid

Info

Publication number
GB406345A
GB406345A GB23742/32A GB2374232A GB406345A GB 406345 A GB406345 A GB 406345A GB 23742/32 A GB23742/32 A GB 23742/32A GB 2374232 A GB2374232 A GB 2374232A GB 406345 A GB406345 A GB 406345A
Authority
GB
United Kingdom
Prior art keywords
acid
chromium
oxide
employed
atmospheres
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB23742/32A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Publication of GB406345A publication Critical patent/GB406345A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

Formic acid is produced by reaction of carbon monoxide with steam in presence of a catalyst comprising a non-volatile acidic oxide not combined with a base or an acid salt derived from an acidic oxide. The acidic oxide may be an oxide of phosphorus, arsenic, tungsten, molybdenum, uranium, chromium, vanadium, titanium, boron, silicon or zirconium, and the acid salts may be primary or secondary phosphates, tungstates or molybdates of zinc, calcium, magnesium, sodium, potassium, copper, cerium or thorium. Mutually combined acid oxides may also be used, such as phosphomolybdic acid, phosphotungstic acid, phosphosilicic acid, silico tungstic acid, silicomolybdic acid, chromium vanadate, or vanadium molybdate. The use of catalysts containing substantial quantities of iron, nickel or cobalt or their compounds is excluded. Carriers such as activated charcoal, fullers earth or kieselguhr may be employed, and inert gases such as nitrogen or carbon dioxide may be present. Pressure is preferably employed, and may be 25--900 atmospheres. The apparatus may be lined with glass or internally coated with chromium or silver or it may be made of acid resisting alloys of molybdenum, cobalt, tungsten, chromium, manganese or nickel. In the examples mixtures of carbon monoxide and steam are passed over (1) an acid zinc phosphate prepared by adding zinc oxide to aqueous phosphoric acid, impregnating a support such as activated charcoal with the solution, and drying at 120 DEG C.; (2) primary calcium phosphate; (3) silicotungstic acid prepared by mixing solutions of sodium tungstate and sodium silicate in equivalent proportions, the mixture being acidified with hydrochloric acid and extracted with ether, the ether being evaporated from the extract and the residue dissolved in water and used to impregnate silica gel; (4) silicomolybdic acid. The pressures employed are respectively 700, 200, 700, and 200 atmospheres and the temperature 325 DEG C. Specifications 29165/10, and 308,666 (as open to inspection under Sect. 91), [both in Class 2 (iii)], are referred to.ALSO:Formic acid is produced by reaction of carbon monoxide with steam in presence of a catalyst comprising a non-volatile acidic oxide not combined with a base or an acid salt derived from an acidic oxide. The acidic oxide may be an oxide of phosphorus, arsenic, tungsten, molybdenum, uranium, chromium, vanadium, titanium, boron, silicon or zirconium, and the acid salts may be primary or secondary phosphates, tungstates or molybdates of zinc, calcium, magnesium, sodium, potassium, copper, cerium or thorium. Mutually combined acid oxides may also be used, such as phosphomolybdic acid, phosphotungstic acid, phosphosilicic acid, silicotungstic acid, silicomolybdic acid, chromium vanadate, or vanadium molybdate. The use of catalysts containing substantial quantities of iron, nickel or cobalt or their compounds is excluded. Carriers such as activated charcoal, fuller's earth or kieselguhr may be employed, and inert gases such as nitrogen or carbon dioxide may be present. Pressure is preferably employed, and may be 25--900 atmospheres. The apparatus may be lined with glass or internally coated with chromium or silver or it may be made of acid resisting alloys of molybdenum, cobalt, tungsten chromium, manganese or nickel. In the examples, mixtures of carbon monoxide and steam are passed over (1) an acid zinc phosphate prepared by adding zinc oxide to aqueous phosphoric acid, impregnating a support such as activated charcoal with the solution, and drying at 120 DEG C.; (2) primary calcium phosphate; (3) silicotungstic acid prepared by mixing solutions of sodium tungstate and sodium silicate in equivalent proportions, the mixture being acidified with hydrochloric acid and extracted with ether, the ether being evaporated from the extract and the residue dissolved in water and used to impregnate silica gel; (4) silicomolybdic acid. The pressures employed are respectively 700, 200, 700, and 200 atmospheres and the temperature 325 DEG C. Specifications 29165/10 and 308,666 (as open to inspection under Sect. 91), [both in [Class 2 (iii)], are referred to.
GB23742/32A 1931-08-24 1932-08-24 Improvements in or relating to the production of formic acid Expired GB406345A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US406345XA 1931-08-24 1931-08-24

Publications (1)

Publication Number Publication Date
GB406345A true GB406345A (en) 1934-02-26

Family

ID=21912073

Family Applications (1)

Application Number Title Priority Date Filing Date
GB23742/32A Expired GB406345A (en) 1931-08-24 1932-08-24 Improvements in or relating to the production of formic acid

Country Status (1)

Country Link
GB (1) GB406345A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7893193B2 (en) 2005-05-20 2011-02-22 Solvay (Société Anonyme) Method for making a chlorohydrin
US7939696B2 (en) 2005-11-08 2011-05-10 Solvay Societe Anonyme Process for the manufacture of dichloropropanol by chlorination of glycerol
US8067645B2 (en) 2005-05-20 2011-11-29 Solvay (Societe Anonyme) Process for producing a chlorhydrin from a multihydroxylated aliphatic hydrocarbon and/or ester thereof in the presence of metal salts
US8124814B2 (en) 2006-06-14 2012-02-28 Solvay (Societe Anonyme) Crude glycerol-based product, process for its purification and its use in the manufacture of dichloropropanol
US8197665B2 (en) 2007-06-12 2012-06-12 Solvay (Societe Anonyme) Aqueous composition containing a salt, manufacturing process and use
US8258350B2 (en) 2007-03-07 2012-09-04 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8273923B2 (en) 2007-06-01 2012-09-25 Solvay (Societe Anonyme) Process for manufacturing a chlorohydrin
US8314205B2 (en) 2007-12-17 2012-11-20 Solvay (Societe Anonyme) Glycerol-based product, process for obtaining same and use thereof in the manufacturing of dichloropropanol
US8378130B2 (en) 2007-06-12 2013-02-19 Solvay (Societe Anonyme) Product containing epichlorohydrin, its preparation and its use in various applications
US8415509B2 (en) 2003-11-20 2013-04-09 Solvay (Societe Anonyme) Process for producing dichloropropanol from glycerol, the glycerol coming eventually from the conversion of animal fats in the manufacture of biodiesel
US8471074B2 (en) 2007-03-14 2013-06-25 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8507643B2 (en) 2008-04-03 2013-08-13 Solvay S.A. Composition comprising glycerol, process for obtaining same and use thereof in the manufacture of dichloropropanol
US8536381B2 (en) 2008-09-12 2013-09-17 Solvay Sa Process for purifying hydrogen chloride
US8715568B2 (en) 2007-10-02 2014-05-06 Solvay Sa Use of compositions containing silicon for improving the corrosion resistance of vessels
US8795536B2 (en) 2008-01-31 2014-08-05 Solvay (Societe Anonyme) Process for degrading organic substances in an aqueous composition
US9309209B2 (en) 2010-09-30 2016-04-12 Solvay Sa Derivative of epichlorohydrin of natural origin
CN112642436A (en) * 2019-10-12 2021-04-13 中石化南京化工研究院有限公司 Catalyst for synthesizing formic acid and preparation method thereof
CN113720987A (en) * 2021-08-11 2021-11-30 信丰华锐钨钼新材料有限公司 Method for removing tungsten, molybdenum, phosphorus and polyacid in tungsten smelting macroporous resin desorption solution
CN116396147A (en) * 2023-03-24 2023-07-07 南京先进生物材料与过程装备研究院有限公司 Novel method for alcohol oxidation reaction with environmental protection and energy saving

Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9663427B2 (en) 2003-11-20 2017-05-30 Solvay (Société Anonyme) Process for producing epichlorohydrin
US8415509B2 (en) 2003-11-20 2013-04-09 Solvay (Societe Anonyme) Process for producing dichloropropanol from glycerol, the glycerol coming eventually from the conversion of animal fats in the manufacture of biodiesel
US8519198B2 (en) 2005-05-20 2013-08-27 Solvay (Societe Anonyme) Method for making an epoxide
US8067645B2 (en) 2005-05-20 2011-11-29 Solvay (Societe Anonyme) Process for producing a chlorhydrin from a multihydroxylated aliphatic hydrocarbon and/or ester thereof in the presence of metal salts
US8106245B2 (en) 2005-05-20 2012-01-31 Solvay (Société Anonyme) Method for preparing chlorohydrin by converting polyhydroxylated aliphatic hydrocarbons
US7893193B2 (en) 2005-05-20 2011-02-22 Solvay (Société Anonyme) Method for making a chlorohydrin
US7906692B2 (en) 2005-05-20 2011-03-15 Solvay (Societe Anonyme) Method for making a chlorohydrin by chlorinating a polyhydroxylated aliphatic hydrocarbon
US8389777B2 (en) 2005-05-20 2013-03-05 Solvay (Société Anonyme) Continuous method for making chlorhydrines
US8420871B2 (en) 2005-05-20 2013-04-16 Solvay (Societe Anonyme) Process for producing an organic compound
US7906691B2 (en) 2005-05-20 2011-03-15 Solvay (Societe Anonyme) Method for making chlorohydrin in corrosion-resistant equipment
US8344185B2 (en) 2005-05-20 2013-01-01 SOLVAY (Société Anonyme Method for making a chlorhydrine by reaction between a polyhydroxylated aliphatic hydrocarbon and a chlorinating agent
US7939696B2 (en) 2005-11-08 2011-05-10 Solvay Societe Anonyme Process for the manufacture of dichloropropanol by chlorination of glycerol
US8106246B2 (en) 2005-11-08 2012-01-31 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol by chlorination of glycerol
US8124814B2 (en) 2006-06-14 2012-02-28 Solvay (Societe Anonyme) Crude glycerol-based product, process for its purification and its use in the manufacture of dichloropropanol
US8258350B2 (en) 2007-03-07 2012-09-04 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8471074B2 (en) 2007-03-14 2013-06-25 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8273923B2 (en) 2007-06-01 2012-09-25 Solvay (Societe Anonyme) Process for manufacturing a chlorohydrin
US8399692B2 (en) 2007-06-12 2013-03-19 Solvay (Societe Anonyme) Epichlorohydrin, manufacturing process and use
US8197665B2 (en) 2007-06-12 2012-06-12 Solvay (Societe Anonyme) Aqueous composition containing a salt, manufacturing process and use
US8378130B2 (en) 2007-06-12 2013-02-19 Solvay (Societe Anonyme) Product containing epichlorohydrin, its preparation and its use in various applications
US8715568B2 (en) 2007-10-02 2014-05-06 Solvay Sa Use of compositions containing silicon for improving the corrosion resistance of vessels
US8314205B2 (en) 2007-12-17 2012-11-20 Solvay (Societe Anonyme) Glycerol-based product, process for obtaining same and use thereof in the manufacturing of dichloropropanol
US8795536B2 (en) 2008-01-31 2014-08-05 Solvay (Societe Anonyme) Process for degrading organic substances in an aqueous composition
US8507643B2 (en) 2008-04-03 2013-08-13 Solvay S.A. Composition comprising glycerol, process for obtaining same and use thereof in the manufacture of dichloropropanol
US8536381B2 (en) 2008-09-12 2013-09-17 Solvay Sa Process for purifying hydrogen chloride
US9309209B2 (en) 2010-09-30 2016-04-12 Solvay Sa Derivative of epichlorohydrin of natural origin
CN112642436A (en) * 2019-10-12 2021-04-13 中石化南京化工研究院有限公司 Catalyst for synthesizing formic acid and preparation method thereof
CN112642436B (en) * 2019-10-12 2023-03-28 中石化南京化工研究院有限公司 Catalyst for synthesizing formic acid and preparation method thereof
CN113720987A (en) * 2021-08-11 2021-11-30 信丰华锐钨钼新材料有限公司 Method for removing tungsten, molybdenum, phosphorus and polyacid in tungsten smelting macroporous resin desorption solution
CN116396147A (en) * 2023-03-24 2023-07-07 南京先进生物材料与过程装备研究院有限公司 Novel method for alcohol oxidation reaction with environmental protection and energy saving
CN116396147B (en) * 2023-03-24 2023-11-10 南京先进生物材料与过程装备研究院有限公司 Alcohol oxidation reaction method

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