CN101070482A - Silica-gel catalyst - Google Patents

Silica-gel catalyst Download PDF

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Publication number
CN101070482A
CN101070482A CNA2007100230446A CN200710023044A CN101070482A CN 101070482 A CN101070482 A CN 101070482A CN A2007100230446 A CNA2007100230446 A CN A2007100230446A CN 200710023044 A CN200710023044 A CN 200710023044A CN 101070482 A CN101070482 A CN 101070482A
Authority
CN
China
Prior art keywords
catalyst
grease
silica gel
oil
methyl alcohol
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.)
Pending
Application number
CNA2007100230446A
Other languages
Chinese (zh)
Inventor
杨贻方
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.)
Wujiang Fangxia Enterprise Information Consultation Co Ltd
Original Assignee
Wujiang Fangxia Enterprise Information Consultation Co Ltd
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 Wujiang Fangxia Enterprise Information Consultation Co Ltd filed Critical Wujiang Fangxia Enterprise Information Consultation Co Ltd
Priority to CNA2007100230446A priority Critical patent/CN101070482A/en
Publication of CN101070482A publication Critical patent/CN101070482A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

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  • Fats And Perfumes (AREA)

Abstract

The invention provides a method of disposing the free fatty acids from oil and fat, it includes the separation, precipitation or conversion of fatty acid. Adjunct consisting of catalyst and dehydrated calcium sulfate powder is put into the solution which includes oil and ethyl alcohol. The oil contains free fatty acids, and the temperature of catalyst is higher than the boiling point of water. After the reaction finished, distilling the catalyst and recover it. Thus, dehydrated calcium sulfate could absorb water of the mixture positively, and makes it lower water amount, while the recovery of catalyst is economical.

Description

Silica-gel catalyst
Technical field
The present invention relates to a kind of biodiesel technology, the chemical industry method of especially greasy conversion biodiesel.
Background technology
In the present greasy transformation technology, carry out in the transesterification reaction at grease and methyl alcohol, 1 mole of grease and 3 mole, of methanol are reacted, and generate 3 moles of methyl esters and 1 mole of glycerin; And in the esterification of lipid acid and methyl alcohol, the reaction of 1 moles of fatty acids and 1 mole, of methanol generates the water of 1 mole of methyl esters and 1 mole.The concentration of the water meeting diluting reaction thing methyl alcohol that generates like this, thus methanol output is reduced greatly, and slowed down reaction speed.
Processing mode is exactly to adopt the method for removing lipid acid at present, can increase technical process and cost like this.
Summary of the invention
The invention provides the simplification technology that a kind of grease transforms, and save cost.
For achieving the above object, technical scheme of the present invention is:
A kind of chemical industry method of greasy conversion biodiesel comprises the reaction of grease and methyl alcohol, it is characterized in that adding Bibulous Silica Gel and methyl acetate catalyzer in grease liquid, methanol liquid slowly is added in the mixing liquid reacts then.
Moisture in the Bibulous Silica Gel active absorption mixture makes methanol solution keep 99% purity, thereby improves methyl esters output and speed of response.
Embodiment
In concrete the enforcement, can have the inorganic salts of crystal water with having added some in the silica gel, as cobalt salt.When anhydrous be exactly state when losing crystal water be blue look, the state when being exactly crystal water during suction is pink.Discolour silica gel can recycle.After colour-change, can in loft drier, toast, make it get back to anhydrous state and just can continue to have used.
Secondly, grease, methyl alcohol, Bibulous Silica Gel and methyl acetate mixture ratio ratio are 12: 2: 1.

Claims (3)

1. the chemical industry method of a greasy conversion biodiesel comprises the reaction of grease and methyl alcohol, it is characterized in that adding Bibulous Silica Gel and methyl acetate catalyzer in grease liquid, methanol liquid slowly is added in the mixing liquid reacts then.
2. according to claim 1, it is characterized in that having the inorganic salts of crystal water with having added some in the silica gel.
3. according to claim 1, it is characterized in that grease, methyl alcohol, Bibulous Silica Gel and methyl acetate mixture ratio ratio are 12: 2: 1.
CNA2007100230446A 2007-05-30 2007-05-30 Silica-gel catalyst Pending CN101070482A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2007100230446A CN101070482A (en) 2007-05-30 2007-05-30 Silica-gel catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2007100230446A CN101070482A (en) 2007-05-30 2007-05-30 Silica-gel catalyst

Publications (1)

Publication Number Publication Date
CN101070482A true CN101070482A (en) 2007-11-14

Family

ID=38897901

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2007100230446A Pending CN101070482A (en) 2007-05-30 2007-05-30 Silica-gel catalyst

Country Status (1)

Country Link
CN (1) CN101070482A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011053175A3 (en) * 2009-10-28 2011-06-23 Instytut Chemii Przemysłowej A method of producing a biofuel for diesel engines

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011053175A3 (en) * 2009-10-28 2011-06-23 Instytut Chemii Przemysłowej A method of producing a biofuel for diesel engines

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Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Open date: 20071114