CPC Corporation

Miaoli, Taiwan

CPC Corporation

Miaoli, Taiwan
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Wiseguyreports.Com Adds “Treated Distillate Aromatic Extract (TDAE) -Market Demand, Growth, Opportunities and Analysis of Top Key Player Forecast To 2022” To Its Research Database Global Treated Distillate Aromatic Extract (TDAE) market competition by top manufacturers/players, with Treated Distillate Aromatic Extract (TDAE) sales volume, Price (USD/MT), revenue (Million USD) and market share for each manufacturer/player; the top players including Geographically, this report split global into several key Regions, with sales (K MT), revenue (Million USD), market share and growth rate of Treated Distillate Aromatic Extract (TDAE) for these regions, from 2012 to 2022 (forecast), covering On the basis of product, this report displays the sales volume (K MT), revenue (Million USD), product price (USD/MT), market share and growth rate of each type, primarily split into High Sulphur Low Sulphur On the basis on the end users/applications, this report focuses on the status and outlook for major applications/end users, sales volume, market share and growth rate of Treated Distillate Aromatic Extract (TDAE) for each application, including Passenger Car Tyre Commercial Car Tyre Global Treated Distillate Aromatic Extract (TDAE) Sales Market Report 2017 1 Treated Distillate Aromatic Extract (TDAE) Market Overview 1.1 Product Overview and Scope of Treated Distillate Aromatic Extract (TDAE) 1.2 Classification of Treated Distillate Aromatic Extract (TDAE) by Product Category 1.2.1 Global Treated Distillate Aromatic Extract (TDAE) Market Size (Sales) Comparison by Type (2012-2022) 1.2.2 Global Treated Distillate Aromatic Extract (TDAE) Market Size (Sales) Market Share by Type (Product Category) in 2016 1.2.3 High Sulphur 1.2.4 Low Sulphur 1.3 Global Treated Distillate Aromatic Extract (TDAE) Market by Application/End Users 1.3.1 Global Treated Distillate Aromatic Extract (TDAE) Sales (Volume) and Market Share Comparison by Application (2012-2022) 1.3.2 Passenger Car Tyre 1.3.3 Commercial Car Tyre 1.4 Global Treated Distillate Aromatic Extract (TDAE) Market by Region 1.4.1 Global Treated Distillate Aromatic Extract (TDAE) Market Size (Value) Comparison by Region (2012-2022) 1.4.2 United States Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.4.3 China Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.4.4 Europe Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.4.5 Japan Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.4.6 Southeast Asia Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.4.7 India Treated Distillate Aromatic Extract (TDAE) Status and Prospect (2012-2022) 1.5 Global Market Size (Value and Volume) of Treated Distillate Aromatic Extract (TDAE) (2012-2022) 1.5.1 Global Treated Distillate Aromatic Extract (TDAE) Sales and Growth Rate (2012-2022) 1.5.2 Global Treated Distillate Aromatic Extract (TDAE) Revenue and Growth Rate (2012-2022) 9 Global Treated Distillate Aromatic Extract (TDAE) Players/Suppliers Profiles and Sales Data 9.1 H&R Group 9.1.1 Company Basic Information, Manufacturing Base and Competitors 9.1.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.1.2.1 Product A 9.1.2.2 Product B 9.1.3 H&R Group Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.1.4 Main Business/Business Overview 9.2 Nynas 9.2.1 Company Basic Information, Manufacturing Base and Competitors 9.2.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.2.2.1 Product A 9.2.2.2 Product B 9.2.3 Nynas Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.2.4 Main Business/Business Overview 9.3 Total 9.3.1 Company Basic Information, Manufacturing Base and Competitors 9.3.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.3.2.1 Product A 9.3.2.2 Product B 9.3.3 Total Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.3.4 Main Business/Business Overview 9.4 CPC Corporation 9.4.1 Company Basic Information, Manufacturing Base and Competitors 9.4.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.4.2.1 Product A 9.4.2.2 Product B 9.4.3 CPC Corporation Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.4.4 Main Business/Business Overview 9.5 IRPC 9.5.1 Company Basic Information, Manufacturing Base and Competitors 9.5.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.5.2.1 Product A 9.5.2.2 Product B 9.5.3 IRPC Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.5.4 Main Business/Business Overview 9.6 CNOOC 9.6.1 Company Basic Information, Manufacturing Base and Competitors 9.6.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.6.2.1 Product A 9.6.2.2 Product B 9.6.3 CNOOC Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.6.4 Main Business/Business Overview 9.7 Shandong Tianyuan Chemical 9.7.1 Company Basic Information, Manufacturing Base and Competitors 9.7.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.7.2.1 Product A 9.7.2.2 Product B 9.7.3 Shandong Tianyuan Chemical Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.7.4 Main Business/Business Overview 9.8 ATDM 9.8.1 Company Basic Information, Manufacturing Base and Competitors 9.8.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.8.2.1 Product A 9.8.2.2 Product B 9.8.3 ATDM Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.8.4 Main Business/Business Overview 9.9 Suzhou Jiutai Group 9.9.1 Company Basic Information, Manufacturing Base and Competitors 9.9.2 Treated Distillate Aromatic Extract (TDAE) Product Category, Application and Specification 9.9.2.1 Product A 9.9.2.2 Product B 9.9.3 Suzhou Jiutai Group Treated Distillate Aromatic Extract (TDAE) Sales, Revenue, Price and Gross Margin (2012-2017) 9.9.4 Main Business/Business Overview For more information, please visit https://www.wiseguyreports.com/sample-request/1082791-global-treated-distillate-aromatic-extract-tdae-sales-market-report-2017


Patent
CPC Corporation and AMT International Inc. | Date: 2013-03-03

Solvent regeneration to recover a polar hydrocarbon (HC) selective solvent substantially free of hydrocarbons (HCs) and other impurities from a solvent-rich stream containing selective solvent, heavy HCs, and polymeric materials (PMs) generated from reactions among thermally decomposed or oxidized solvent, heavy HCs, and additives is provided. A combination of displacement agent and associated co-displacement agent squeezes out the heavy HCs and PMs from the extractive solvent within a solvent clean-up zone. Simultaneously, a filter equipped with a magnetic field is positioned in a lean solvent circulation line to remove paramagnetic contaminants. The presence of the co-displacement agent significantly enhances the capability of the displacement agent in removing the heavy HCs and PMs from the extractive solvent. As a result, the solvent regeneration system operates under milder conditions and minimizes or eliminates the need for including a high temperature, energy intensive and difficult-to-operate thermal solvent regenerator.


Patent
CPC Corporation and AMT International Inc. | Date: 2013-02-20

Extractive distillation processes whereby water-soluble extractive distillation (ED) solvents are regenerated and recovered employ improved operations of the extractive distillation column (EDC) so that polar hydrocarbons are recovered and purified from mixtures containing polar and less polar hydrocarbons and measurable amounts of hydrocarbons that are heavier than intended feedstock and/or polymers that are generated in the ED process. The improved process can effectively remove and recover the heavy hydrocarbons and/or remove polymer contaminants from the solvent in a closed solvent circulating loop through mild operating conditions with no additional process energy being expended. With the improved process, the overhead reflux of the EDC may be eliminated to further reduce energy consumption and to enhance the loading and performance within the upper portion of the EDC, especially when two liquid phases exists therein.


Patent
CPC Co. | Date: 2016-09-07

Disclosed is a suction plate, and more particularly to a suction plate, in which a pad (10) to which a suction band (30) is attached along an outer bottom surface is pressed down by external force while contacting a target surface (s) and then restored upward when released from the external force, so that a vacuum can be created between a center portion (11) of the pad and the target surface since the outer portion of the pad is firmly attached to the target surface by the suction band and the center portion having no suction band tends to move upward by the restoring force when a user presses the pad against the target surface and releases the pad, thereby strongly attaching the pad to the target surface.


A silicon resin composition, transparent optical film, and packaging materials manufactured thereby are provided. The silicon resin composition has (A) silicone and (B) metal oxide-polymer oligomer particles. The (B) metal oxide-polymer oligomer particles are in the amount of 0.5 to 5 wt % of the total weight of the silicon resin composition. The silicon resin composition has the property of low thermal stress, high refractive index, transparency, heat resistance and good adhesion, and can be widely used in different applications.


Patent
CPC Corporation | Date: 2013-10-17

A process for converting paraffin by using a modified zirconia catalyst is provided. The process has steps of: (i) providing feed containing n-pentane, n-hexane and more than 2 vol % n-heptane based on the volume of the feed; and (ii) subjecting the feed to isomerization of n-heptane with a modified zirconia catalyst comprising zirconium oxide, sulfate ions, a first metal component and a second metal component. Based on the weight of the catalyst, an amount of the first metal component ranges between 0.1 wt % and 15 wt %, an amount of the second metal component ranges between 0.2 wt % and 3.0 wt %, and an amount of the sulfate ions contain sulfur is less than 1.0 wt %. By using the modified zirconia catalyst with low sulfate content, the process is beneficial to improve iso-C_(7 )selectivity and conversion rate in heptane isomerization.


Patent
CPC Corporation | Date: 2014-08-28

A method for making high purity dicyclopentadiene comprises the following steps: providing a dimer feedstock comprising dicyclopentadiene and methyl dicyclopentadiene; blending the dimer feedstock and a diluent to obtain a first blend; cracking the first blend in a vapor phase at 300 C. to 400 C. to obtain a cracked feedstock; separating the cracked feedstock into a second blend and a third blend; dimerizing the second blend at 50 C. to 120 C. to obtain a fourth blend; and separating the fourth blend to obtain a recycled diluent and high purity dicyclopentadiene. By using saturated C5 hydrocarbon, saturated C6 hydrocarbon, benzene and the mixture thereof as the diluent and the steps mentioned above, the clogging problem of cracker tubes is solved and the cost of makeup diluent usage is lowered.


Patent
Cpc Corporation | Date: 2014-11-18

A method for producing adamantane includes the steps of preparing a catalytic composition including an acidic ionic liquid and a co-catalyst and subjecting a tetrahydrodicyclopentadiene-containing component to isomerization in the presence of the catalytic composition to form adamantane. The acidic ionic liquid includes aluminum chloride and a quaternary onium compound selected from the group consisting of a quaternary ammonium halide, a quaternary phosphonium halide, and a combination thereof. The co-catalyst is an oxygen-containing reagent.


This invention describes a method for co-producing isobutene and methyl tert-butyl ether in a catalytic distillation column, wherein contacting with solid acid catalysts the charged tert-butanol mixture undergoes dehydration and etherification. The mixture of isobutene and methyl tert-butyl ether withdrawn from the column top can be further separated, thus high purity isobutene and fuel-additive methyl tert-butyl ether are obtained.


A dual-bed catalytic distillation tower has a catalytic column having an upper catalytic bed filled with low temperature dehydration catalysts and a lower catalytic bed filled with high temperature dehydration catalysts. When using the dual-bed catalytic distillation tower, the feeding may be fed to the tower at the top of the upper catalytic bed, between the upper and lower catalytic beds, or at the bottom of the lower catalytic bed for dehydration to obtain DME. The dual-bed catalytic distillation tower has the advantage of flexible set-up depending on various feedings such as anhydrous or crude methanol and on different grades of DME to be obtained.

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