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  • Users: Canoman
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  1. Canoman

    Thermal Relief Question

    I'm looking at an existing thermal relief valve and trying to calculate a relief load for it. (The client doesn't have this information). The valve is on the cooling water (tubeside) side of a shell and tube exchanger. The case I'm examining is a blocked exit of the cooling water, while the...
  2. Canoman

    Perry's Table Typo?

    I'm looking at Perry's 7th Ed., Table 2-5, Vapor Pressure of Liquid Water from 0 to 100°C. Is this a typo? 33.2°C, Pvap = 38.155 mmHg 33.3°C, Pvap = 38.369 mmHg 33.4°C, Pvap = 33.584 mmHg (Should this be 38.584??) 33.5°C, Pvap = 38.801 mmHg 33.6°C, Pvap = 39.018 mmHg 33.7°C, Pvap = 39.237 mmHg...
  3. Canoman

    Briefly exceeding flange ratings?

    Are there any guidelines anywhere that would say if it's alright to exceed flange ratings in an upset case? My client has installed a new pump, and we are designing a vessel that goes downstream of the pump. In order to set the design pressure of this vessel, I've investigated two cases. One...
  4. Canoman

    Design & Relieving Temperatures

    I had originally specified a small vessel (filter shell) with a design pressure of 150psig and a design temperature of 350°F, but after looking more closely at the specified pump and the PSV loads, I realized that the design temperature and pressure might need to be changed. I changed the...
  5. Canoman

    Repeating rows @ bottom of each page

    Does anyone know how to repeat rows at the bottom of each printed page in Excel? I have a 412 character text string that I want to be repeated on the bottom of each page, but the footer will only allow me to use 255 characters. If I could somehow insert an image file into the footer, I could...
  6. Canoman

    MDEA Viscosity

    I've been looking for some data on MDEA viscosity at low temperatures. As of yet, the lowest temperature that I have found any data for is 32°F. I want some data so that I can show the need for steam tracing piping through which pure, or almost pure, MDEA flows. The ambient temperature can...
  7. Canoman

    PSV Sizing: Double Jeopardy??

    When sizing a PSV, there are a number of cases that one must consider. Blocked exit is just one of them. I am looking at the blocked exit case for sizing a relief valve on a trayed amine absorber. The feed is a header system in which a few streams combine before flowing into the absorber. Of...
  8. Canoman

    Off the wall question about brain freezes

    I'm a chemical engineer who's always been interested in applying chemical engineering thinking towards things in the body. I took a few classes in college that gave me a "biomedical" specialty within chemical engineering, but my current job has nothing to do with bio stuff. Anyway, I...
  9. Canoman

    API Pump Specs

    Anyone know of a website that lists API Pump specs such as A-8, S-1, S-6, etc. and what each of them means? I know that one of these designations basically specifies all materials in a pump, but I do not know what each spec means. When we do equipment lists, we show things like "Carbon...
  10. Canoman

    Eductor sales

    Can anyone let me know some companies that make eductors/ejectors other than Schutte & Koerting, Penberthy and Jacoby-Tarbox? If possible, could I get a phone number and/or website address? Thanks Canoman
  11. Canoman

    Steam quality from a boiler

    Does anyone know of a good method to calculate the quality of steam leaving the disengagement space of a waste heat boiler? The boiler recovers heat from reactor effluent and produces steam to cool the process gas. I am looking for a method on how to figure out how much water is entrained in...

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