By Timothy Adam

ISBN-10: 0470944560

ISBN-13: 9780470944561


In an international the place such a lot items are synthetic via machines, Etsy deals a web platform for makers of home made items and crafts to marketplace and promote their items to an enormous community of dealers who call for specified, actual items. so far, the location has attracted over 400,000 who jointly have offered over 30 million goods, producing greater than $180.6 million in profit. the one source of its variety, tips to earn cash utilizing Etsy--written through Tim Adam who has effectively been promoting his items around the world via his Etsy store due to the fact that 2007--guides readers step by step during the many levels of promoting on-line. How-to subject matters include:
Establish your Etsy shop
Effectively picture your products
Post your items to optimize visibility and raise sales
Brand your business
Use social media like blogs, Twitter, and fb to hook up with purchasers and develop your enterprise

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38]. 39]. Numerous procedures for preparing mixtures of methanol and higher alcohols, including butanols, are presently under development (so-called fuel methanol). 40]. 14; the large fraction of C4 -alcohols is noteworthy. 14. 41] Component weight % C) alcohol C2 alcohol C3 alcohol C4 alcohol Csalcohol ketones and aldehydes water 68-72 2-3 3-5 10-15 7-12 max. 2 max. 5 bar. 42]. 43]. Despite its advantages (no hydrogen needed, favourable n: i ratio) the procedure has found only a single operator, Japan Butanol (30,000 tla).

No secondary processes using pure 2-butenes are known so that it is better to separate first i-butane and then I-butene in two successive fractionations. 30]. Krupp-Koppers is running a pilot plant in Essen for extractive distillation of C4 components from various C4 -streams. By means of the extraction agent Butenex it was possible to separate raffinate I into the fractions butaneslbutenes , and raffinate II into butanes/l-butenel2-butene. trans-2-Butene can be largely separated from nbutane but it is not possible to separate i-butene and I-butene.

This was developed by Ruhrchemie in 1938, and involves treating propene with about equimolar amounts of carbon monoxide and hydrogen on metalcarbonyl catalysts at 90 to 180°C and 25 to 350 bar. This yields a mixture of the butanals; the ratio of n-: i-isomers can be regulated from 1: 1 to 20: 1 by choice of catalyst and reaction conditions. 36]: or CH 3 ....... CH-CHO CH3/ The yield is 90 to 98%. The highest possible proportion of n-butanal is aimed to match existing consumption patterns. Recently this has been accomplished with modified Rh-catalysts at low pressure.

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How to Make Money Using Etsy: A Guide to the Online Marketplace for Crafts and Handmade Products by Timothy Adam

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