Answer:
I think for this would most likely have to be C
Explanation:
I'd have to say that since if you were to keep calling people out for it it sorta defeats the purpose? something like that-
Answer:
d. Making the guest welcome, making the operation run correctly, keeping control operating costs.
Explanation:
The basic work of managers in the hospitality industry calls for: Making the guest welcome, making the operation run correctly, keeping control operating costs.
The hospitality industry's backbone is comprised of customer service, it is the foundation and cornerstone of all segments of the industry. A business may focus on one or all facets of hospitality but the level of success achieved is dependent on how well the managers and staff, are serving their customers.
Answer:
$73,600
Explanation:
Cash flow from Operating Activity
Cash sales $26,000
Collections on accounts receivable $99,000
Payments to suppliers ($47,000)
Cash generated from operations $78,000
Income taxes paid ($4,400)
Net cash provided by operating activities $73,600
therefore,
the amount of net cash provided by operating activities indicated by these transactions is $73,600
A filmmaker will seek a sound production mixer who has the qualities and qualifications that is responsible for ensuring that dialogue recorded during filming is suitably clear, tries to avoid unwanted noises and works around the camera which might hamper the placement of microphones. A production sound mixer who has his or her own equipment as this choice can save the filmmaker a considerable amount of money in sound equipment rental, and the mixer is likely to be skilled in using his or her own equipment.
We are given the series of chemical reactions:
Ethane is chlorinated in a continuous reactor:
C2H6 + Cl2 --> C2H5Cl + HCl
But some of the product monochloroethane becomes further
chlorinated by an undesired side reaction:
C2H5Cl + Cl2 --> C2H4Cl2 + HCl
So to avoid the product monochloroethane to be further
chlorinated, there must be fast processing or fast conversion of ethane so that
there would less time for further chlorination. Hence we must design the
reactor for high conversion of ethane.
To make the process economical, there must be a
downstream separation step that would separate the main product monochloroethane
from the undesired product dichloroethane.