Thermax. D Ltd. is an Indian energy and environment engineering company based in India and Britain. It manufactures, boilers, vapour absorption machines, offers water and waste solutions and installs captive power projects. Thermax is also a historic brand name of boilers, and the name of a former toughened-glass company.Anu Aga was the chairperson of the company 1996–2004, till she handed over the reins to her daughter, Meher Pudumjee, and figured amongst the eight richest Indian women, and in 2007 was part of 40 Richest Indians by net worth according to Forbes magazine, in 2009 she was at number 55, and continues to be a board member. Wikipedia.


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The absorption chiller-heater apparatus of present invention utilizes a portion of direct heat, used to heat water, for providing the refrigeration effect. The external heat input required for providing refrigeration is minimal; hence, the efficiency of the apparatus is increased by 30 - 40 % over the conventional systems. Further, as the quantum of the external heat source required for a new cycle is reduced, the size of the high temperature generator (102) required, is smaller, which results in lower capital costs. The apparatus provides chilled water which can be used for various industrial purposes. The absorption chiller-heater reduces CO_(2) emissions and utilizes a single arrangement to produce both heating and refrigeration effect. Thus, additional electrical and heat input or separate components are not required.


Patent
Thermax | Date: 2011-11-29

The present invention envisages a hybrid absorption-compression chiller comprising: a vapor-compression system providing refrigeration effect in a primary evaporator (102a) by extracting heat from a medium to be cooled in a condensed primary refrigerant, and a vapor-absorption system in operative communication with the vapor-compression system for receiving primary refrigerant vapors via a compressor (104a), these vapors are cooled by a condensed secondary refrigerant in a secondary evaporator (106a) to provide cold condensed primary refrigerant which is recycled to the vapor-compression system. The hybrid absorption-compression chiller of the present invention is energy-efficient and provides a higher COP in comparison with the conventional chillers.


Patent
Thermax | Date: 2012-06-22

A triple-effect vapor absorption refrigeration system is disclosed. The system comprises a high temperature generator, a medium temperature generator, and a low temperature generator, for concentrating a dilute LiBr solution from an absorber, through a flow path from the high temperature generator to the low temperature generator via the medium temperature generator. In the system maximum LiBr solution temperature and maximum LiBr solution concentration does not occur simultaneously, hence, LiBr corrosion rate is reduced and minimum non-condensable gases are generated, this helps in maintaining vacuum during operation thus providing a smoother operation.


Monomer solution and liquid solution immiscible with the monomers in the monomer solution are cocurrently jetted upwardly in a pulsating manner in a reaction vessel. Monomer droplets are allowed to rise up in a controlled and smooth manner under the dynamic forces exerted by differential flow rate and differential pressure between the monomer and liquid solutions and the differential densities between the monomer and liquid solutions without causing coalescence, agglomeration and breakup of the monomer droplets and to stabilize by partial polymerization of the droplets at 50-60 C. The monomer droplets flow out horizontally into a polymerization reactor and get polymerized in the polymerization reactor under agitation at 80-85 C. The polymer beads are dried at 80-100 C. and sieved.


Monomer solution and liquid solution immiscible with the monomers in the monomer solution are cocurrently jetted upwardly in a pulsating manner in a reaction vessel. Monomer droplets are allowed to rise up in a controlled and smooth manner under the dynamic forces exerted by differential flow rate and differential pressure between the monomer and liquid solutions and the differential densities between the monomer and liquid solutions without causing coalescence, agglomeration and breakup of the monomer droplets and to stabilize by partial polymerization of the droplets at 50-60 C. The monomer droplets flow out horizontally into a polymerization reactor and get polymerized in the polymerization reactor under agitation at 80-85 C. The polymer beads are dried at 80-100 C. and sieved.


Grant
Agency: Cordis | Branch: FP7 | Program: CP-SICA | Phase: ENERGY.2011.6.1-1 | Award Amount: 5.30M | Year: 2011

The OPTIMASH project aims to optimise the efficiency and reliability of gasifiers fuelled with high-ash content coals. High Pressure Circulating Fluidized Bed gasifiers are the target technology. The objective of this 4 years project is to develop a pilot gasifier capable of producing a syngas flow at 10 bars suitable for 1MWth. The gasification characteristics of high ash content coal will be investigated using pressurized Drop Tube Furnace facilities and accompanying measurement instruments. Coal gasification models will be developed taking into account the relevant chemical kinetics. In parallel, coal beneficiation and preparation studies will be conducted experimentally; the results will be modelled for their generalization. The 1 MWth pilot-scale plant will be modelled and numerically simulated using relevant CFD codes. The computations will be validated with data coming from the pilot-plant. The global IGCC system using the developed gasifier will be modelled using existing energy and mass balance soft-wares. Commercial scale design criteria will be developed taking into account pressure and geometric scaling. Indian high ash coals are the main target of the project. To insure the fuel flexibility of the developed process, Turkish high ash coals will also be studied and their characteristics used in the modelling of the process. The project will allow optimizing the global efficiency of the gasification technology for high ash coal by minimizing the steam use, optimising particle size vs residence time, developing particle agglomeration avoidance strategies, investigating corrosion risks, increasing fuel flexibility, developing efficient ash disposal system and testing different technologies for gas cooling, tar and fly ash removal. The consortium comprises a major industrial partner and a major research institute from India, together with two major research organisms from Netherlands and France, the Turkish Coal Enterprises and one Turkish university.


Patent
Thermax | Date: 2013-01-23

A triple-effect vapor absorption refrigeration system (100) is disclosed. The system (100) comprises a high temperature generator (102), a medium temperature generator (104), and a low temperature generator (106), for concentrating a dilute Li-Br solution from an absorber (110), through a flow path from the high temperature generator (102) to the low temperature generator (106) via the medium temperature generator (104). In the system (100) maximum Li-Br solution temperature and maximum Li-Br solution concentration does not occur simultaneously, hence, Li-Br corrosion rate is reduced and minimum non-condensable gases are generated, this helps in maintaining vacuum during operation thus providing a smoother operation.


Patent
Thermax | Date: 2011-02-23

The absorption chiller-heater apparatus of present invention utilizes a portion of direct heat, used to heat water, for providing the refrigeration effect. The external heat input required for providing refrigeration is minimal; hence, the efficiency of the apparatus is increased by 30-40% over the conventional systems. Further, as the quantum of the external heat source required for a new cycle is reduced, the size of the high temperature generator required, is smaller, which results in lower capital costs. The apparatus provides chilled water which can be used for various industrial purposes. The absorption chiller-heater reduces CO_(2 )emissions and utilizes a single arrangement to produce both heating and refrigeration effect. Thus, additional electrical and heat input or separate components are not required.


Method and apparatus for preparing polymer beads of uniform particle size by suspension polymerization. A monomer solution of polymerizing monomers containing initiators is jetted into an upwardly flowing stream of monomer droplets through a plurality of orifices of 50-300 micron sizes at the bottom of a vertically located monomer droplets forming reaction vessel in a pulsating manner at a flow rate of 2-4 litrs per hr and at a pressure of 0.2 to 1 Kg/cm^(2) and simultaneously a liquid solution immiscible with the monomers and containing suspension stabilizers is cocurrently jetted into an upwardly flowing stream through a plurality of holes of 0.5 - 1 mm sizes at the bottom of the reaction vessel spaced above and around the outer periphery of the orifices in a pulsating manner at a flow rate of 4-8 litrs per hr and at a pressure of 2.5 to 3 Kg/cm^(2). The ratio between the monomer solution and the liquid solution is 1:10 v/v and the holes are spaced above the orifices at a distance of 10-40mm. The monomer droplets in the liquid solution are allowed to rise up in the reaction vessel in a controlled and smooth manner under the dynamic forces exerted by differential flow rate and differential pressure between the pulsating monomer solution and liquid solution supplies and the differential densities between the monomer and liquid solutions without causing coalescence, agglomeration and breakup of the monomer droplets and to stabilize by partial polymerization of the droplets by the suspension stabilizers in the liquid solution at 50 to 60C in the reaction vessel. The monomer droplets in the liquid solution are allowed to flow out from the reaction vessel horizontally into a polymerization reactor fitted with agitator and located at an elevated position with respect to the reaction vessel and get polymerized in the polymerization reactor at 80-85C. The polymer beads are dried at 80 to 100C and sieved. The invention is simple to carry out, reduces energy requirement and cycle time and is cost effective.


News Article | February 16, 2017
Site: marketersmedia.com

This report studies sales (consumption) of Steam Trap in Global market, especially in North America, Europe, China, Japan, Southeast Asia and India, focuses on top players in these regions/countries, with sales, price, revenue and market share for each player in these regions, covering Market Segment by Regions, this report splits Global into several key Regions, with sales (consumption), revenue, market share and growth rate of Steam Trap in these regions, from 2011 to 2021 (forecast), like Split by product types, with sales, revenue, price, market share and growth rate of each type, can be divided into Type I Type II Type III Split by applications, this report focuses on sales, market share and growth rate of Steam Trap in each application, can be divided into Application 1 Application 2 Application 3 1 Steam Trap Overview 1.1 Product Overview and Scope of Steam Trap 1.2 Classification of Steam Trap 1.2.1 Type I 1.2.2 Type II 1.2.3 Type III 1.3 Applications of Steam Trap 1.3.1 Application 1 1.3.2 Application 2 1.3.3 Application 3 1.4 Steam Trap Market by Regions 1.4.1 North America Status and Prospect (2011-2021) 1.4.2 China Status and Prospect (2011-2021) 1.4.3 Europe Status and Prospect (2011-2021) 1.4.4 Japan Status and Prospect (2011-2021) 1.4.5 Southeast Asia Status and Prospect (2011-2021) 1.4.6 India Status and Prospect (2011-2021) 1.5 Global Market Size (Value and Volume) of Steam Trap (2011-2021) 1.5.1 Global Steam Trap Sales, Revenue and Price (2011-2021) 1.5.2 Global Steam Trap Sales and Growth Rate (2011-2021) 1.5.3 Global Steam Trap Revenue and Growth Rate (2011-2021) 9 Global Steam Trap Manufacturers Analysis 9.1 Armstrong 9.1.1 Company Basic Information, Manufacturing Base and Competitors 9.1.2 Steam Trap Product Type and Technology 9.1.2.1 Type I 9.1.2.2 Type II 9.1.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.2 CIRCOR 9.2.1 Company Basic Information, Manufacturing Base and Competitors 9.2.2 Steam Trap Product Type and Technology 9.2.2.1 Type I 9.2.2.2 Type II 9.2.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.3 Flowserve 9.3.1 Company Basic Information, Manufacturing Base and Competitors 9.3.2 Steam Trap Product Type and Technology 9.3.2.1 Type I 9.3.2.2 Type II 9.3.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.4 Pentair 9.4.1 Company Basic Information, Manufacturing Base and Competitors 9.4.2 Steam Trap Product Type and Technology 9.4.2.1 Type I 9.4.2.2 Type II 9.4.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.5 Spirax Sarco 9.5.1 Company Basic Information, Manufacturing Base and Competitors 9.5.2 Steam Trap Product Type and Technology 9.5.2.1 Type I 9.5.2.2 Type II 9.5.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.6 Aman Engineering Works 9.6.1 Company Basic Information, Manufacturing Base and Competitors 9.6.2 Steam Trap Product Type and Technology 9.6.2.1 Type I 9.6.2.2 Type II 9.6.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2016) 9.7 Beijing Convista Flow Control Equipment 9.7.1 Company Basic Information, Manufacturing Base and Competitors 9.7.2 Steam Trap Product Type and Technology 9.7.2.1 Type I 9.7.2.2 Type II 9.7.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2017) 9.8 Bestobell 9.8.1 Company Basic Information, Manufacturing Base and Competitors 9.8.2 Steam Trap Product Type and Technology 9.8.2.1 Type I 9.8.2.2 Type II 9.8.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2018) 9.9 D-KTC 9.9.1 Company Basic Information, Manufacturing Base and Competitors 9.9.2 Steam Trap Product Type and Technology 9.9.2.1 Type I 9.9.2.2 Type II 9.9.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2019) 9.10 Forbes Marshall 9.10.1 Company Basic Information, Manufacturing Base and Competitors 9.10.2 Steam Trap Product Type and Technology 9.10.2.1 Type I 9.10.2.2 Type II 9.10.3 Steam Trap Sales, Revenue, Price of Company One (2015 and 2021) 9.11 GESTRA 9.12 Mahavas Precision Controls 9.13 Miyawaki 9.14 Thermax 9.15 TLV 9.16 Velan 9.17 Watson McDaniel 9.18 Yoshitake For more information, please visit https://www.wiseguyreports.com/sample-request/606750-global-steam-trap-sales-market-report-2021

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