Esterification unit for producing crude methyl methacrylate, esterification process using said unit and plant comprising said unit
US-10131614-B2 · Nov 20, 2018 · US
US9932291B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9932291-B2 |
| Application number | US-201515521440-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 13, 2015 |
| Priority date | Oct 27, 2014 |
| Publication date | Apr 3, 2018 |
| Grant date | Apr 3, 2018 |
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Fouling of an MMA process is reduced by acidifying a stream comprising recycled components.
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What is claimed is: 1. A process for producing methyl methacrylate (MMA) comprising: (a) contacting methacrylamide with methanol in an aqueous reaction medium in an esterification reaction zone in the presence of an acidic raw material comprising sulfuric acid to produce a first stream comprising MMA, water, methanol, the acidic raw material and methacrylic acid (MAA); (b) phase separating the first stream into a first aqueous stream comprising the acidic raw material, and a first organic liquid product stream comprising MMA, methanol and MAA; (c) neutralizing the MAA of the first organic liquid product stream with ammonia to produce a neutralized stream comprising MMA, methanol and ammonium methacrylate; (d) optionally adding water to the neutralized stream; (e) separating the neutralized stream into a second organic stream comprising MMA, and a second aqueous stream comprising methanol and ammonium methacrylate; (f) contacting the second aqueous stream with an acidifying agent to form an acidified aqueous stream; and (g) sending at least a portion of the acidified aqueous stream to the reaction zone, wherein the amount of acidifying agent admixed with the second aqueous stream is an amount sufficient to acidify the second aqueous stream to a pH of less than 1.75 before it reaches the reaction zone. 2. The process of claim 1 wherein the separating of step (e) comprises at least one of distillation and phase separation. 3. The process of claim 1 wherein the separating of step (e) comprises phase separation. 4. The process of claim 1 wherein the acidifying agent comprises fresh acid or acid taken from another process stream. 5. The process of claim 4 wherein the acidifying agent comprises acid from another process stream. 6. The process of claim 4 wherein the acidifying agent comprises fresh acid. 7. The process of claim 1 wherein the contacting the second aqueous stream with an acidifying agent to form an acidified aqueous stream comprises admixing the acidifying agent with the second aqueous stream via a static mixer. 8. The process of claim 3 wherein the phase separation is conducted in a decanter, the acidic raw material comprises sulfuric acid, the acidifying agent comprises sulfuric acid, and the amount of acidifying agent is an amount sufficient to acidify the second aqueous stream to a pH of less than 1.75 before it reaches the reaction zone. 9. The process of claim 8 wherein the amount of acidifying agent is an amount sufficient to acidify the second aqueous stream to a pH of less than or equal to 1.5 before it reaches the reaction zone.
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