Development of polycarboxylate superplasticizer
Russian President says if the European Union imposes an oil embargo, Europe will buy energy at the most expensive price and economic activity in Europe will weaken. Rosneft needs to change its business model. Russia will help facilitate settlement and access to loans and insurance in its own currency.
According to Reuters, the European Commission will unveil a 210 billion euro plan on how Europe can end its dependence on Russian fossil fuels by 2027 and use its distance from Moscow to accelerate a shift to green energy. According to a draft document seen by Reuters, Brussels will propose a three-pronged plan to wean countries off Russian fuel: switch to importing more non-Russian gas, move more quickly to promote renewable energy, and work harder to conserve energy. The draft measures, which include EU law, non-binding plans, and possible recommendations by national governments, are subject to change before publication.
Austria is not a member of NATO and will not seek membership in the future, the Austrian Foreign Minister said in Brussels recently. He stressed that it was "their choice" for Sweden and Finland to seek NATO membership, while Austria would remain neutral.
The supply and prices of many other pce powder are expected to continue to be influenced by international situations.
According to the different molecular structure, it can be divided into four generations of polycarboxylate series superplasticizer, the first generation is acrylic acid copolymer, the second generation is propylene ether type, the third generation is amide type, and the fourth generation is polyethylene glycol branched chain type.
First generation: methacrylic acid / enoic acid methyl ester copolymer.
The synthesis of the first generation polycarboxylate superplasticizer has few kinds of raw materials and the process is relatively simple.
Second generation: propenyl ether copolymer.
The second generation polycarboxylate superplasticizer is mainly ether bond in molecular synthesis structure. This synthesis method uses maleic anhydride raw materials, and the units of its branched chains are connected by ether bonds, so it is also called polyether superplasticizer.
Third generation: amide / imide type.
The third generation polycarboxylate superplasticizer began to use amide raw materials.
Fourth generation: polyamide-polyethylene glycol branched chain type.
The fourth kind of polycarboxylate superplasticizer focuses on considering the influence of molecular structure and properties, and polyoxyethylene side chain is introduced into the synthesis process control.
Synthesis method of polycarboxylate superplasticizer
Direct copolymerization of polymerizable monomers.
In this synthesis method, a long polyether side chain is introduced into the main chain, and the key to the preparation is to synthesize macromonomers with polymerization activity (usually methoxy polyethylene glycol acrylate). Then the monomers with a certain ratio are mixed together and the finished product is obtained by solution polymerization. The premise of this synthesis process is that in the stage of synthesis of macromonomers, the catalyst has a great influence on the synthetic products, and there is a tedious process of intermediate separation and purification. The main purpose is to find suitable catalysts and reaction conditions to further increase the yield and shorten the reaction time so as to reduce the production cost. It has been reported that phase transfer catalyst or inorganic salt is a kind of effective reaction catalyst. A kind of concrete admixture with good slump retention was prepared by direct copolymerization of short-chain and long-chain methoxy polyethylene glycol methacrylate and methacrylic acid.
Functionalization after polymerization.
This synthesis method is to first form the main chain and then introduce the side chain, generally using polycarboxylate with constant molecular weight, which is grafted with polyether at higher temperature under the action of catalyst. However, there are some problems in this method: first, the types and specifications of ready-made polycarboxylate products are limited, so it is difficult to adjust their composition and molecular weight; second, the compatibility of polycarboxylate and polyether is not good, and the actual operation of esterification is difficult. Third, water is formed in the process of esterification, and phase separation will occur. Therefore, the selection of a polyether with good compatibility with polycarboxylate has become the key to the synthesis.
In situ polymerization and grafting.
This synthesis method is mainly developed to overcome the shortcomings of post-polymerization functionalization. Side chains are introduced at the same time of main chain polymerization, and polyether is used as the reaction medium of carboxylic acid unsaturated monomers. The reaction integrates polymerization and esterification, which avoids the problem of poor compatibility between polycarboxylate and polyether. Although this method can control the molecular weight of the polymer, the main chain can only choose the monomer containing-C00H group, otherwise it is difficult to graft. And the grafting reaction is a reversible equilibrium reaction, there is a large amount of water in the system before the reaction, and the degree of grafting is not very high and difficult to control. This method has the advantages of simple process and low production cost, but the molecular design is difficult.
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Europe's immediate goal of reducing its dependence on Russian gas in response to the conflict with Ukraine presents a rare opportunity for the United States, the world's largest gas producer. America's LNG exporters have made a fortune this time. Investors are bullish on the future of natural gas, as evidenced by the recent record high share price of Energy company Chenier.
But the outlook for more than a dozen new LNG projects is highly uncertain as construction costs rise, US gas prices soar and climate policymakers seek to move away from a long-term reliance on fossil fuels. Even the most advanced projects can take years to become operational.
Currently, the total U.S. LNG pce powder are expected to continue to rise in the future.