CN109647521B - Catalyst for preparing polyformaldehyde dimethyl ether - Google Patents
Catalyst for preparing polyformaldehyde dimethyl ether Download PDFInfo
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- CN109647521B CN109647521B CN201710941274.4A CN201710941274A CN109647521B CN 109647521 B CN109647521 B CN 109647521B CN 201710941274 A CN201710941274 A CN 201710941274A CN 109647521 B CN109647521 B CN 109647521B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
- B01J31/08—Ion-exchange resins
- B01J31/10—Ion-exchange resins sulfonated
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/30—Ion-exchange
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/48—Preparation of compounds having groups
- C07C41/50—Preparation of compounds having groups by reactions producing groups
- C07C41/56—Preparation of compounds having groups by reactions producing groups by condensation of aldehydes, paraformaldehyde, or ketones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/40—Substitution reactions at carbon centres, e.g. C-C or C-X, i.e. carbon-hetero atom, cross-coupling, C-H activation or ring-opening reactions
- B01J2231/42—Catalytic cross-coupling, i.e. connection of previously not connected C-atoms or C- and X-atoms without rearrangement
- B01J2231/4277—C-X Cross-coupling, e.g. nucleophilic aromatic amination, alkoxylation or analogues
- B01J2231/4288—C-X Cross-coupling, e.g. nucleophilic aromatic amination, alkoxylation or analogues using O nucleophiles, e.g. alcohols, carboxylates, esters
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Abstract
The invention relates to a catalyst for preparing polyformaldehyde dimethyl ether, which mainly solves the problems of low catalyst activity and low selectivity in the process of synthesizing the polyformaldehyde dimethyl ether by taking methanol, methylal and paraformaldehyde as reaction raw materials in the prior art.
Description
Technical Field
The invention relates to a catalyst for preparing polyoxymethylene dimethyl ether.
Background
In recent years, with the influence of industrial revolution, the petroleum resources in China are increasingly tense and the pressure of petroleum supply is unprecedentedly increased along with the unique resource pattern of 'more coal, less oil and gas'. The petroleum supply rate in China is only 50% in the future 10-20 years. How to solve the energy crisis of China by using abundant coal resources of China becomes a problem which needs to be solved urgently by researchers. Therefore, people pay more attention to the development of novel oil substitutes from coal-based methanol.
Dimethyl ether was originally proposed as an additive for diesel fuel, but the cost of dimethyl ether as an alternative fuel for vehicles is significantly increased due to its poor cold start performance, high vapor pressure at normal temperature and easy generation of vapor lock. Polyoxymethylene dimethyl ethers (PODE) is a generic term for a class of substances, and can be represented by the general formula CH3O(CH2O)nCH3Having a higher octane number (>30) And oxygen content (42-51%). When the value of n is 2-10, the physical property and the combustion performance of the dimethyl ether are very close to those of diesel oil, and the defects of dimethyl ether as a blending component of the vehicle diesel oil are overcome. Therefore, the polyoxymethylene dimethyl ether can be used as a novel clean diesel component, the addition amount in the diesel can reach 30 percent (v/v), the combustion condition of the diesel in an engine can be improved, the thermal efficiency is improved, and particles in tail gas are reducedSubstance and COxAnd NOxAnd (4) discharging. Reportedly, 5-30% CH is added3OCH2OCH3Can reduce NOxThe emission is 7-10%, and the PM is reduced by 5-35%. The PODE synthesized by the coal-based methanol can replace part of diesel oil, improve the combustion efficiency of the diesel oil, reduce the harm of the combustion of the diesel oil to the environment, and has important strategic significance and good economic value.
CN 101048357a (method for preparing polyoxymethylene dimethyl ether) introduces a method for synthesizing polyoxymethylene dimethyl ether by using methylal and trioxymethylene as reactants and using inorganic acid, sulfonic acid, heteropoly acid, acidic ion exchange resin, zeolite, alumina, etc. as catalysts. However, the conversion and selectivity of the existing catalysts are to be improved.
The cation exchange resin as solid acid catalyst shows excellent catalytic reaction performance in esterification and etherification reaction of water-containing system, but the acid strength is lower. It is common to prepare supported resins, the activity of which is enhanced by increasing the acidity of the catalyst. The metal modified resin can be adopted to form a new acid center on the catalyst, and the new acid center can not be exchanged by other metal ions, so that the problem that the acidity of the catalyst can not be replaced by metal ions contained in raw materials to be inactivated under the condition that the catalyst keeps high activity in industrial application of polyformaldehyde dimethyl ether synthesis is solved.
Disclosure of Invention
One of the technical problems to be solved by the invention is that the problem of low selectivity of n-2-10 products exists in the process of synthesizing polyoxymethylene dimethyl ether by taking methanol, methylal and paraformaldehyde as reaction raw materials in the prior art, and a novel catalyst for preparing polyoxymethylene dimethyl ether is provided. The catalyst has the advantage of high product selectivity of n-2-10.
The second technical problem to be solved by the present invention is to provide a method for preparing the catalyst by using the first technical problem.
The third technical problem to be solved by the present invention is the application of the catalyst described in one of the above technical problems.
In order to solve one of the above technical problems, the technical solution of the present invention is as follows:
the catalyst for preparing the polyoxymethylene dimethyl ether is cation exchange resin modified by metal ions, and the modified metal comprises IIA metal. The modified sulfonic acid type polystyrene cation exchange resin obviously improves the selectivity of PODE (potassium peroxidase) with n being 2-10.
In the above technical solution, the modified metal includes Ga.
In the above technical solution, the IIA metal is preferably at least one selected from Ra, Be, Mg, Ca, Sr, and Ba.
In the technical scheme, the modified metal further comprises Ga and IIA metal, and the Ga and the IIA metal have a synergistic effect in the aspect of improving the selectivity of PODE (peroxidase) with n being 2-10. The ratio between Ga and IIA metals is not particularly limited, as long as a comparable synergistic effect is achieved with both Ga and IIA metals present in the catalyst.
The mass ratio of Ga to IIA metal is, by way of non-limiting example, 0.01 to 100, and further non-limiting examples within this range include 0.1, 0.5, 0.8, 1, 1.5, 2, 3, 4, 5, 6, 7, 8, 9, 10, and the like.
In the technical scheme, the modified metal comprises at least two of IIA metals, such as but not limited to Ra and Be, Mg and Ca, Sr and Ba, and every two of the IIA metals have synergistic effect on improving selectivity of PODE (potassium peroxidase) on n-2-10. At this time, the ratio between Ra and Be, Mg and Ca, Sr and Ba is not particularly limited as long as the above-mentioned two IIA metal elements are present in the catalyst at the same time to obtain a comparable synergistic effect.
As non-limiting examples, the mass ratio between Ra and Be, Mg and Ca, Sr and Ba is 0.01-100, and further non-limiting examples within this range include 0.1, 0.5, 0.8, 1, 1.5, 2, 3, 4, 5, 6, 7, 8, 9, 10, and the like.
In the above-mentioned technical solution, the content of the modified metal in the catalyst is not particularly limited, but is not limited to, for example, the content of the modified metal in the catalyst is more than 0 and 9.8w% or less.
In the technical scheme, the total exchange capacity of the resin is 3.0-5.9 mmol/g.
In the above technical solution, the resin may be of a gel type or a macroporous type.
In the above technical solution, the resin is preferably sulfonic acid type polystyrene cation exchange resin.
In the above technical scheme, the sulfonic acid type polystyrene comprises a crosslinked polystyrene skeleton and a sulfonic acid group.
In order to solve the second technical problem, the technical scheme of the invention is as follows:
the method for preparing a catalyst according to any one of the above technical problems, comprising contacting the cation exchange resin with a suspension containing the modified metal oxide and/or hydroxide in the presence of a catalytic amount of an acid to effect ion exchange.
In the above technical scheme, the acid is not particularly limited as long as the salt obtained by the reaction with the modified metal oxide and/or hydroxide can be dissolved in the solvent used for the suspension, and in this principle, for example, but not limited to, at least one of hydrochloric acid, nitric acid, and C2 to C10 carboxylic acids.
In the above technical scheme, the carboxylic acid may be a hydroxy-substituted carboxylic acid, such as but not limited to glycolic acid, lactic acid, tartaric acid, citric acid, and the like.
In the above technical scheme, the carboxylic acid may be a C2-C10 monobasic acid, such as but not limited to acetic acid and the like.
In order to solve the third technical problem, the technical scheme of the invention is as follows:
the application of the catalyst in the technical scheme of one of the technical problems in synthesizing polyoxymethylene dimethyl ether.
The polyformaldehyde dimethyl ether can be synthesized by taking methanol, methylal and paraformaldehyde as raw materials, wherein the mass ratio of the methanol to the methylal to the paraformaldehyde is (0-10) to 1, the using amount of the methanol and the methylal cannot be 0 at the same time, and the raw materials are contacted with the catalyst to react to generate the polyformaldehyde dimethyl ether.
In the technical scheme, the dosage of the catalyst is preferably 0.05-10% of the weight of the raw materials; more preferably 0.1 to 5% by weight of the raw material.
In the technical scheme, the reaction temperature is preferably 70-200 ℃.
In the technical scheme, the reaction pressure is preferably 0.2-6 MPa.
In the above technical scheme, the reaction time is preferably 1 to 20 hours, more preferably 4 to 12 hours.
In the technical scheme, the mass ratio of the sum of the using amounts of methanol and methylal in the raw materials to paraformaldehyde is preferably (0.4-5) to 1; the mass ratio of the methanol to the methylal to the paraformaldehyde is (0.2-10) to (0.5-10) to 1.
In the case where the composition of the catalyst of the present invention has been clarified, the preparation of the catalyst is not particularly limited and can be carried out by referring to an ion exchange method which is generally used in the prior art. For example, the following steps can be included: washing the sodium sulfonate type polystyrene cation exchange resin with deionized water until clear water flows out, soaking the resin in 0.5-20% strong acid (such as hydrochloric acid or sulfuric acid) for 1-12 h, soaking the resin in deionized water or an ethanol solution for 1-12 h, and then washing the resin with deionized water until the pH value is 6, thus obtaining the sulfonic acid type polystyrene cation exchange resin. While the sulfonic acid type polystyrene cation exchange resin of the present invention is also directly available from commercial sources, it can be used for the preparation of the catalyst of the present invention, rather than the sodium sulfonate type.
By adopting the catalyst, the yield of PODE with n-2-10 is good, the selectivity of the product with n-2-10 is as high as 89.6%, and a better technical effect is achieved.
The total exchange capacity in the present invention is based on dry resin.
The present invention is further illustrated by the following examples, wherein the polymerization degree of the raw material paraformaldehyde used in the examples and comparative examples is 5, and the product selectivity is calculated by taking paraformaldehyde as a reference and taking polyoxymethylene dimethyl ether with the polymerization degree of 2-10 as a target product.
Detailed Description
[ example 1 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin on a dry basis were taken and 300ml of Ga (OH) containing 2 g of Ga3Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 2 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic acid polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ra (OH) 2 g of Ra under nitrogen protection2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with Ra content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 3 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to the dry resin, and mixing with 300ml of Be (OH) containing 2 g of Be under the protection of nitrogen2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Be content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 4 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking a pictureWhen 98 g of sulfonic acid polystyrene cation exchange resin is dry, the resin is mixed with 300ml of Mg (OH) containing 2 g of Mg under the protection of nitrogen2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Mg content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 5 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ca (OH) containing 2 g of Ca under nitrogen protection2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ca content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 6 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to the dry resin is taken and mixed with 300ml of Sr (OH) containing 2 g of Sr under the protection of nitrogen2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Sr content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 7 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic acid polystyrene cation exchange resin corresponding to the dry resin was taken and mixed with 300ml of Ba (OH) containing 2 g of Ba under nitrogen protection2Mixing the water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ba content of 2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 8 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to dry resin, and reacting with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Ra under the protection of nitrogen3And Ra (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Ra content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 9 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 deg.C to obtain the final productThe sulfonic acid type polystyrene cation exchange resin has a total exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to the dry resin, and mixing with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Be under the protection of nitrogen3And Be (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Be content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 10 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to dry resin, and reacting with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Mg under the protection of nitrogen3And Mg (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Mg content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 11 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to dry resin, and mixing with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Ca under the protection of nitrogen3And Ca (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Ca content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 12 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to the dry resin, and mixing with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Sr under the protection of nitrogen3And Sr (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Sr content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 13 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to dry resin, and mixing with 300ml of Ga (OH) containing 1 g of Ga and 1 g of Ba under the protection of nitrogen3And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w% and the Ba content of 1 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 14 ]
1. Preparation of the catalyst
Sulfonic acidThe sodium polystyrene cation exchange resin 7320 is washed by deionized water until clear water flows out, and is soaked by 4 w% hydrochloric acid for four times, 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium polystyrene cation exchange resin 7320 is used for each time, the sodium polystyrene cation exchange resin is soaked for 4h, then the sodium polystyrene cation exchange resin is washed by deionized water until no chloride ion exists in the eluate, and the sodium polystyrene cation exchange resin is dried at 60 ℃ to obtain the sulfonic polystyrene cation exchange resin, wherein the total exchange capacity of the sulfonic polystyrene cation exchange resin is 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.5 g of Ra and 0.5 g of Be under nitrogen protection3、Ra(OH)2And Be (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.5 w% and the Be content of 0.5 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 15 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.5 g of Mg and 0.5 g of Ca under nitrogen protection3、Mg(OH)2And Ca (OH)2Mixing the mixed aqueous suspensions, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hr, and vacuum-filteringDrying the mixture in a drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Mg content of 0.5 w% and the Ca content of 0.5 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 16 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic acid polystyrene cation exchange resin corresponding to the dry resin is taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.5 g of Sr and 0.5 g of Ba under the protection of nitrogen3、Sr(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Sr content of 0.5 w% and the Ba content of 0.5 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 17 ]
1. Preparation of the catalyst
Sodium sulfonate type polystyrene cation exchange resin7320 washing with deionized water until clear water flows out, soaking with 4 w% hydrochloric acid for four times, each time using 4 w% hydrochloric acid 10 times of the dry weight of 7320, soaking for 4h, washing with deionized water until the eluate has no chloride ion, and drying at 60 deg.C to obtain sulfonic polystyrene cation exchange resin with total exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.4 g of Ra, 0.3 g of Be and 0.3 g of Mg under nitrogen protection3、Ra(OH)2、Be(OH)2And Mg (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.4 w%, the Be content of 0.3 w% and the Mg content of 0.3 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 18 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking 98 g of sulfonic acid type polystyrene cation exchange resin corresponding to the dry resin, and mixing with 300ml of Ga (OH) containing 1 g of Ga, 0.4 g of Ca, 0.3 g of Sr and 0.3 g of Ba under the protection of nitrogen3、Ca(OH)2、Sr(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of iceAcetic acid, mixing, standing for 24 hours at room temperature, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ca content of 0.4 w%, the Sr content of 0.3 w% and the Ba content of 0.3 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 19 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.25 g of Ra, 0.25 g of Be, 0.25 g of Mg and 0.25 g of Ca under the protection of nitrogen3、Ra(OH)2、Be(OH)2、Mg(OH)2And Ca (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.25 w%, the Be content of 0.25 w%, the Mg content of 0.25 w% and the Ca content of 0.25 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 20 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to the dry resin is taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.25 g of Ra, 0.25 g of Be, 0.25 g of Sr and 0.25 g of Ba under the protection of nitrogen3、Ra(OH)2、Be(OH)2、Sr(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.25 w%, the Be content of 0.25 w%, the Sr content of 0.25 w% and the Ba content of 0.25 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 21 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. Taking the same as the stem base tree98 g of a sulfonic acid polystyrene cation exchange resin to 300ml of Ga (OH) containing 1 g of Ga, 0.25 g of Mg, 0.25 g of Ca, 0.25 g of Sr and 0.25 g of Ba under nitrogen protection3、Mg(OH)2、Ca(OH)2、Sr(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Mg content of 0.25 w%, the Ca content of 0.25 w%, the Sr content of 0.25 w% and the Ba content of 0.25 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 22 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to the dry resin was mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.2 g of Ra, 0.2 g of Be, 0.2 g of Mg, 0.2 g of Ca and 0.2 g of Sr under the protection of nitrogen3、Ra(OH)2、Be(OH)2、Mg(OH)2、Ca(OH)2And Sr (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.2 w%, the Be content of 0.2 w%, the Mg content of 0.2 w%, the Ca content of 0.2 w% and the Sr content of 0.2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 23 ]
1. Preparation of the catalyst
Washing the sodium sulfonate type polystyrene cation exchange resin 7320 with deionized water until clear water flows out, soaking for four times with 4 w% hydrochloric acid, soaking for 4h each time with 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320, washing with deionized water until the eluate has no chloride ions, and drying at 60 ℃ to obtain the sulfonic type polystyrene cation exchange resin with the full exchange capacity of 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin was mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.2 g of Ra, 0.2 g of Be, 0.2 g of Mg, 0.2 g of Ca and 0.2 g of Ba under nitrogen protection3、Ra(OH)2、Be(OH)2、Mg(OH)2、Ca(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.2 w%, the Be content of 0.2 w%, the Mg content of 0.2 w%, the Ca content of 0.2 w% and the Ba content of 0.2 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ example 24 ]
1. Preparation of the catalyst
Sodium sulfonateThe type polystyrene cation exchange resin 7320 is washed by deionized water until clear water flows out, and is soaked by 4 w% hydrochloric acid for four times, 4 w% hydrochloric acid which is 10 times of the dry weight of the sodium sulfonate type polystyrene cation exchange resin 7320 is used for each time, the soaking time is 4h, then the washing liquid is washed by the deionized water until no chloride ion exists in the washing liquid, and the sulfonic acid type polystyrene cation exchange resin is obtained after the drying at 60 ℃, wherein the full exchange capacity of the sulfonic acid type polystyrene cation exchange resin is 4.10 mmol/g. 98 g of sulfonic polystyrene cation exchange resin corresponding to dry resin is taken and mixed with 300ml of Ga (OH) containing 1 g of Ga, 0.2 g of Ra, 0.2 g of Be, 0.15 g of Mg, 0.15 g of Ca, 0.15 g of Sr and 0.15 g of Ba under the protection of nitrogen3、Ra(OH)2、Be(OH)2、Mg(OH)2、Ca(OH)2、Sr(OH)2And Ba (OH)2Mixing the mixed water suspension, adding 1 drop of glacial acetic acid, mixing, standing at room temperature for 24 hours, and drying in a vacuum drying oven to constant weight to obtain the catalyst with the Ga content of 1 w%, the Ra content of 0.2 w%, the Be content of 0.2 w%, the Mg content of 0.15 w%, the Ca content of 0.15 w%, the Sr content of 0.15 w% and the Ba content of 0.15 w%.
2. Synthesis of polyformaldehyde dimethyl ether
2 g of catalyst, 100 g of methanol and 100 g of paraformaldehyde are added into a 300ml tank reactor, the mixture is reacted for 4 hours at 130 ℃ and 0.5MPa autogenous pressure, and a sample is extracted, centrifuged and analyzed by gas chromatography. The product contains the dimethyl ether of paraformaldehyde and unreacted raw materials of methanol and polyformaldehyde, and the composition distribution is shown in table 1.
[ COMPARATIVE EXAMPLE 1 ]
The same ratio as in example 1 was used except that the catalyst used was 2 g of the dry sulfonic acid type polystyrene cation exchange resin described in example 1 and the other process conditions were the same as in example 1, and the results are shown in Table 1.
TABLE 1
n is polymerization degree, and the product is CH3O(CH2O)nCH3。
Claims (9)
1. The catalyst for preparing the polyoxymethylene dimethyl ether is a cation exchange resin modified by metal ions, the modified metal comprises IIA metal and Ga, and the IIA metal is at least one selected from Be, Mg, Ca, Sr and Ba.
2. The catalyst of claim 1 wherein the amount of modifying metal in the catalyst is greater than 0 and not greater than 9.8% by weight.
3. The catalyst according to claim 1, wherein the resin has a total exchange capacity of 3.0 to 5.9 mmol/g.
4. The catalyst according to claim 1, wherein the resin is of the gel type or macroporous type.
5. The catalyst according to claim 1, wherein the resin is a polystyrene cation exchange resin of sulfonic acid type.
6. The catalyst of claim 5, wherein the sulfonic acid type polystyrene comprises a crosslinked polystyrene backbone and sulfonic acid groups.
7. A process for preparing a catalyst as claimed in any one of claims 1 to 6, which comprises ion-exchanging the cation exchange resin in contact with a suspension containing the modified metal oxide and/or hydroxide in the presence of a catalytic amount of acid.
8. The method of claim 7, wherein the acid is at least one of hydrochloric acid, nitric acid, and C2-C10 carboxylic acid.
9. Use of the catalyst of any one of claims 1 to 6 in the synthesis of polyoxymethylene dimethyl ethers.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL159360B (en) * | 1968-06-24 | 1979-02-15 | Sir Soc Italiana Resine Spa | PROCESS FOR PREPARING ACRYLIC ACID AND / OR METHACRYLIC ACID. |
| CN1506444A (en) * | 2002-12-13 | 2004-06-23 | 中国石油天然气股份有限公司 | Catalytically cracking process of modifying gasoline |
| CN106582834A (en) * | 2015-10-16 | 2017-04-26 | 中国石油化工股份有限公司 | Catalyst for preparation of polyoxymethylene dimethyl ether |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL159360B (en) * | 1968-06-24 | 1979-02-15 | Sir Soc Italiana Resine Spa | PROCESS FOR PREPARING ACRYLIC ACID AND / OR METHACRYLIC ACID. |
| CN1506444A (en) * | 2002-12-13 | 2004-06-23 | 中国石油天然气股份有限公司 | Catalytically cracking process of modifying gasoline |
| CN106582834A (en) * | 2015-10-16 | 2017-04-26 | 中国石油化工股份有限公司 | Catalyst for preparation of polyoxymethylene dimethyl ether |
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